JPH07126911A - Spinneret for melt spinning - Google Patents

Spinneret for melt spinning

Info

Publication number
JPH07126911A
JPH07126911A JP5273993A JP27399393A JPH07126911A JP H07126911 A JPH07126911 A JP H07126911A JP 5273993 A JP5273993 A JP 5273993A JP 27399393 A JP27399393 A JP 27399393A JP H07126911 A JPH07126911 A JP H07126911A
Authority
JP
Japan
Prior art keywords
yarn
spinneret
spinning
blocks
melt
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.)
Pending
Application number
JP5273993A
Other languages
Japanese (ja)
Inventor
Taketoshi Sugimoto
武敏 杉本
Masami Sasaki
正美 佐々木
Mitsutaka Kageyama
充孝 影山
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.)
Toray Industries Inc
Original Assignee
Toray Industries Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toray Industries Inc filed Critical Toray Industries Inc
Priority to JP5273993A priority Critical patent/JPH07126911A/en
Publication of JPH07126911A publication Critical patent/JPH07126911A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To provide a melt-spinning spinneret capable of spinning a plural kinds of yarns of wide yarn variety with a single spinneret at the same time by opening nozzle holes on a circular spinneret in the form of blocks having specific arrangement and spacings between holes for each yarn. CONSTITUTION:Nozzle holes 2 are opened on a circular spinneret 1 having a diameter (a) of 70-140mm in the form of blocks for respective yarns. The gap (b) between the blocks is 8-35mm and the number of blocks is 2-4. The nozzle holes of each block are arranged in alternate zigzag form on the cross points of plural parallel linear line groups having a spacing (c) of 5-10mm and >=4 parallel linear line groups having a spacing (d) of 3-10mm. The number of nozzle holes on each block is 12-100. The chimney cooling air is blown in the direction of the arrow 3 to minimize the generation of turbulent air flow and enable stable melt-spinning of a yarn having a filament fineness of 0.5-20d.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は溶融口金に関するもので
あり、更に詳しくは、紡糸中に単糸干渉を生じることな
く安定して紡糸可能なフィラメント用の溶融紡糸口金に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a melt spinneret, and more particularly to a melt spinneret for filaments which can be stably spun without causing single yarn interference during spinning.

【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、編物等の原料して広く利用されており、近年の
傾向としてソフトな風合を追求した細単糸デニール多フ
ィラメント糸や機能性を追求した太単糸デニール寡フィ
ラメント糸の市場ニーズが高まってきている。細単糸デ
ニール多フィラメント糸を製造する方法としては、口金
の単位面積当りの吐出孔数を可能な限り多くし、吐出孔
から吐出された溶融ポリマー状の条件を単糸干渉を生じ
ることなく一定の短時間巾に、均一に冷却固化させて、
制電性および平滑性の付与等を目的に紡糸油剤を給油し
て巻取る方法が一般的であり、単糸干渉を生じることな
く、均一に冷却固化する方法について従来より多数の技
術が開示されている。
2. Description of the Related Art Synthetic fibers such as polyester and polyamide are widely used as raw materials for woven fabrics, knitted fabrics, etc. In recent years, fine single yarn denier multifilament yarns and functionality have been pursued in pursuit of soft texture. The market needs for thick single yarn denier wool filament yarn are increasing. As a method for producing thin single-filament denier multifilament yarn, the number of discharge holes per unit area of the die is increased as much as possible, and the condition of the molten polymer discharged from the discharge holes is kept constant without causing single-thread interference. For a short period of time, uniformly cool and solidify,
A method of supplying a spinning oil and winding the same for the purpose of imparting antistatic property and smoothness is generally used, and many techniques have been disclosed as to a method of uniformly cooling and solidifying without causing single yarn interference. ing.

【0003】例えば特公昭47−2047号公報および
特公昭54−36691号公報では複数の同心円上に吐
出孔を放射状若しくは千鳥状に配列した該口金を用いた
紡糸方法が開示されているが、同心円上に配列した口金
の場合、同心円の数が多く同心円の間隔もせまいため、
冷却風の通りが不十分で、短時間に均一に冷却固化する
のがむずかしく従って、糸斑や染着斑を生じやすい。ま
た冷却強化のためと冷却風量を増加すると単糸干渉を生
じて糸切れを生じる等の欠点があった。
For example, Japanese Patent Publication No. 47-2047 and Japanese Patent Publication No. 54-36691 disclose a spinning method using a spinneret in which ejection holes are arranged in a radial or zigzag pattern on a plurality of concentric circles. In the case of the bases arranged above, the number of concentric circles is large and the intervals between concentric circles are small, so
The passage of cooling air is insufficient, and it is difficult to uniformly cool and solidify in a short time. Therefore, yarn spots and dyeing spots are likely to occur. In addition, there is a defect that, for the purpose of strengthening the cooling and when the cooling air volume is increased, single yarn interference occurs and yarn breakage occurs.

【0004】また、特開平5−33209号公報、特開
平5−125609号公報および特開平5−17150
6号公報では細デニー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均一な製品を得る方法が開示され
ているがこれらの開示技術で示されている口金や方法で
溶融吐出ポリマーが細化し、冷却固化が完了するまでに
単糸干渉を生じることなく安定に生産できる糸種の範囲
は単糸デニ―ルが1.0d以下の超細単糸デニールの領
域であり、単糸デニールが1.5d以上になると前記従
来技術と同様に溶融吐出ポリマーが細化し、冷却固化が
完了するまでに単糸干渉を生じて紡糸糸切れを生じると
いう欠点を有している。
Further, JP-A-5-33209, JP-A-5-125609 and JP-A-5-17150.
No. 6 discloses a method for obtaining a fine denier multifilament yarn efficiently and with a good process condition to obtain a uniform product. However, the melt-discharging polymer is thinned by the spinneret and method shown in these disclosed techniques. The range of yarn types that can be stably produced without causing interference of single yarns by the completion of cooling and solidification is the range of ultra-fine single yarn denier with single yarn denier of 1.0d or less, and single yarn denier of 1 If it is 0.5 d or more, the melt-discharge polymer is thinned as in the prior art, and there is a drawback that single yarn interference occurs and spinning yarn breakage occurs by the time the cooling and solidification are completed.

【0005】他方、太単糸デニール寡フィラメント糸を
紡糸する方法としては多フィラメント糸の場合に比較し
て、吐出孔間隔が単糸干渉を生じないだけの十分な距離
を確保しやすいため、例えば特公昭47−8764号公
報に開示されているような従来技術でも十分に対応可能
である。しかし乍ら、これらの従来技術では1口金で単
糸条のマルチフィラメント糸を紡糸する使用法であり、
生産性が低いと云う欠点がある。生産性を高めるために
1口金で複数の糸条を紡糸する多糸条紡糸法を採用する
場合には太単糸デニール寡フィラメント糸の場合にも多
フィラメント糸の場合と同様に従来技術では、溶融吐出
ポリマーが細化し、冷却固化が完了するまで単糸干渉を
生じることなく紡糸することができないという大きな欠
点を有している。
On the other hand, as a method of spinning a thick single-filament denier-oligo filament yarn, as compared with the case of a multi-filament yarn, it is easy to secure a sufficient distance between discharge holes so as not to cause single yarn interference. The conventional technique disclosed in Japanese Examined Patent Publication No. Sho 47-8764 is also sufficient. However, these prior arts have a method of spinning a single filament multifilament yarn with one spinneret,
It has the drawback of low productivity. In the case of employing a multi-spindle spinning method in which a plurality of yarns are spun by a single spinneret in order to enhance productivity, in the case of a thick single yarn denier egofilament yarn as well as in the case of a multifilament yarn, in the prior art, It has a major drawback that the melt-discharged polymer becomes fine and cannot be spun without causing single yarn interference until cooling and solidification are completed.

【0006】[0006]

【本発明が解決しようとする課題】本発明の目的は上記
従来技術の課題を解消せんとするものであり、従来から
広く用いられている円形の紡糸口金の直行する直線上の
交点に吐出孔を千鳥状に交互配列することによって、冷
却風が溶融吐出された個々の単位に当って生じる乱気流
の発生を最小限に抑制することで、個々の単糸の不規則
なゆれをなくすとともに、冷却風のスムーズな流れを可
能にしたことで均一な冷却が可能になり、従って単糸干
渉を生じることなく生産が可能な糸種の単糸デニールの
範囲が0.5〜20dと極めて広い領域で安定した生産
が可能な溶融紡糸口金を提供せんとするものである。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems of the prior art. A discharge hole is formed at an intersection point on a straight line of a circular spinneret which has been widely used in the past. By staggering them in a zigzag pattern, the generation of turbulence that occurs when the cooling air hits the individual units melted and discharged is suppressed to a minimum, eliminating irregular fluctuations of individual single yarns and cooling. The smooth flow of the wind enables uniform cooling, and thus the range of single yarn denier of the yarn types that can be produced without causing single yarn interference is in an extremely wide range of 0.5 to 20d. It is intended to provide a melt-spinning spinneret capable of stable production.

【0007】[0007]

【課題を解決するための手段】すなわち、本発明は直径
ammの円形の紡糸口金に吐出孔をブロック配列し、各
ブロックの間隔がbmmである多糸条同時紡糸口金にお
いて、吐出孔が繰り返し周期cmmで平行な2本以上の
直線群と該直線群に交叉する繰り返しdmmで4本以上
の平行な直線群によって形成される交点上に千鳥状に交
互配列され、かつ下記条件で満たしていることを特徴と
する溶融紡糸口金である。 (1) 70≦a≦140 (2) 8≦b≦35 (3) 5≦c≦10 (4) 3≦d≦10 (5) 2≦ブロック数≦4 (6) 12≦各ブロックの吐出孔数≦100 以下本発明を図面に基づいて具体的に説明する。
That is, according to the present invention, in a multi-spindle simultaneous spinneret in which discharge holes are arranged in blocks in a circular spinneret having a diameter of amm, and the intervals between the blocks are bmm, the discharge holes are repeatedly cycled. staggered on the intersection formed by two or more groups of parallel straight lines of cmm and four or more groups of parallel straight lines intersecting the straight line group, and satisfying the following conditions Is a melt-spinning spinneret. (1) 70 ≤ a ≤ 140 (2) 8 ≤ b ≤ 35 (3) 5 ≤ c ≤ 10 (4) 3 ≤ d ≤ 10 (5) 2 ≤ number of blocks ≤ 4 (6) 12 ≤ discharge of each block Number of Holes ≦ 100 Hereinafter, the present invention will be specifically described with reference to the drawings.

【0008】図1は本発明の2糸条同時紡糸口金の1実
施例を示す概略図、図2は比較例として従来技術の同心
円等配列吐出孔の2糸条同時紡糸口金の1実施例を示す
概略図である。
FIG. 1 is a schematic view showing an embodiment of a two-thread simultaneous spinning spinneret of the present invention, and FIG. 2 is a comparative example of one embodiment of a two-thread simultaneous spinning spinneret having concentric circles and equidistant discharge holes. It is a schematic diagram showing.

【0009】本発明に係わる溶融紡糸口金は、図1に示
すように直径が70〜140mmの口金に吐出孔が各糸
条毎にブロック配列され、各ブロックの間隔(分離帯)
が8〜35mmであり、各ブロックの吐出孔が繰り返し
周期5〜10mmの平行な2本以上の直接群と該直接群
に交叉する繰り返し周期3〜10mmで4本以上の平行
な直線群によって形成される交点上に千鳥状に交互配列
されており、糸条を形成するブロック数が2〜4個であ
り、各ブロックの吐出孔数が12〜100個であること
を意味する。口金直径70〜140mmであるのは、7
0mm未満では本発明の吐出孔配列を有する糸条同時紡
糸口金の作製が実質的に困難になり、他方140mm以
上では口金面積が大きくなりすぎるため、口金を取り付
ける装置も大型化により経済効果が相殺されるようにな
るため口金直径は70〜140mmでなければならな
い。吐出孔が各糸条毎にブロック配列され、各ブロック
の間隔が8〜35mmであるのは、溶融紡糸の際に各糸
条毎に分割して巻き取る必要があり、正確な分割の作業
性を確保するために各ブロックの間隔が8mm以上必要
であり、他方35mm以上になると吐出孔配置面積が減
少し、実質的に本発明の口金を製作するのが困難になる
ため各ブロックの間隔は8〜35mmでなければならな
い、各ブロックの吐出孔が繰り返し周期5〜10mmの
平行な2本以上の直線群と該直線群に交叉する繰り返し
周期3〜10mmで4本以上の平行な直線群によって形
成される交点上に千鳥状に交互配列するのは各ブロック
の分離帯に平行な直線群の間隔が5mm未満では冷却風
の通り抜けが不充分により特に単糸デニールが3d 以上
の糸種では糸ゆれが増加して糸斑が増加するとともに単
糸干渉が生じ断糸トラブルが発生するようになるため、
5mm以上好ましくは6mm以上必要であり、他方、1
0mm以上になると吐出孔の有効配置面積が小さくな
り、十分な吐出孔数を維持できなくなるため、各ブロッ
クの分離帯に平行な直線群の間隔は5〜10mm好まし
くは6〜10mmでなければならない、また、各ブロッ
クの分離帯に平行な直線群に交叉する直線群の繰り返し
周期3〜10mmであるのは3mm未満では糸ゆれによ
る単糸干渉が生じ易く、特に単糸デニールが3d以上の
糸種では断糸トラブルが発生するため、3mm以上好ま
しくは5mm以上、更に好ましくは6mm以上必要であ
り、他方、10mm以上になると吐出孔の有効配置面積
が小さくなり、十分な吐出孔数を維持できなくなるた
め、10mm以下でなければならない。
In the melt-spinning spinneret according to the present invention, as shown in FIG. 1, discharge holes are arranged in blocks for each yarn in a spinneret having a diameter of 70 to 140 mm, and the intervals between the blocks (separation zones).
Is 8 to 35 mm, and the discharge holes of each block are formed by two or more parallel direct groups each having a repeating cycle of 5 to 10 mm and four or more parallel linear groups intersecting the direct group at a repeating cycle of 3 to 10 mm. The number of blocks forming the yarns is 2 to 4, and the number of discharge holes of each block is 12 to 100. The diameter of the base is 70 to 140 mm, 7
If it is less than 0 mm, it will be substantially difficult to produce a yarn simultaneous spinning spinneret having the discharge hole arrangement of the present invention. On the other hand, if it is 140 mm or more, the area of the spinneret will be too large. The diameter of the die must be 70-140 mm in order to be processed. The discharge holes are arranged in blocks for each yarn, and the interval between the blocks is 8 to 35 mm, because it is necessary to divide each yarn during winding during melt spinning, and the workability of accurate division is high. In order to secure the above, the distance between the blocks is required to be 8 mm or more. On the other hand, when the distance is 35 mm or more, the discharge hole disposition area is reduced, and it becomes substantially difficult to manufacture the die of the present invention. The discharge holes of each block must have a length of 8 to 35 mm, and a group of two or more parallel straight lines having a repeating period of 5 to 10 mm and a group of four or more parallel straight lines intersecting the straight line group at a repeating period of 3 to 10 mm. The staggered alternate arrangement on the formed intersections is because if the distance between the groups of straight lines parallel to the separation zone of each block is less than 5 mm, the passage of the cooling air is insufficient, especially in the case of single yarn denier yarn types of 3d or more. More shaking Since the single yarn interference occurs yarn breakage trouble with the yarn unevenness is increased so generated and,
5 mm or more, preferably 6 mm or more, on the other hand, 1
If it is 0 mm or more, the effective arrangement area of the discharge holes becomes small and it becomes impossible to maintain a sufficient number of discharge holes. Therefore, the interval of the straight line groups parallel to the separation band of each block must be 5 to 10 mm, preferably 6 to 10 mm. Further, the repeating period of the straight line group intersecting with the straight line group parallel to the separation band of each block is 3 to 10 mm. If the length is less than 3 mm, the single yarn interference due to the yarn deviation easily occurs, and particularly, the yarn having a single yarn denier of 3d or more is used. Since the yarn breakage trouble occurs in the case of 3 kinds, it is necessary to be 3 mm or more, preferably 5 mm or more, more preferably 6 mm or more, while if it is 10 mm or more, the effective arrangement area of the discharge holes becomes small, and a sufficient number of discharge holes can be maintained. Since it disappears, it must be 10 mm or less.

【0010】各々の直線群の本数が2本以上および4本
以上であるのは、必要に応じて十分な吐出孔数を確保す
るためである。また、各々の直線群の交叉角度は垂直が
最も好ましいが、垂直±45℃の範囲での斜交であって
もよい。また、各々の直線群によって形成される交点上
に吐出孔を千鳥状に交互配列するのは糸ゆれによる単糸
干渉を回避するためである。糸ゆれは冷却風による糸の
吹流によって生じる水平方向の力と下方へ引き取られる
ために生じる垂直方向の力のバランスが崩れて生じる前
後方向の糸ゆれと糸が空気中を高速で通過するために生
じる空気抵抗によって生じる空気流に冷却風の流れが作
用して生じる左右方向の糸ゆれが合成して発生してお
り、糸斑や断糸トラブル等の実害を生じる単糸干渉を回
避するためには、隣接する前後左右の吐出孔間隔が十分
に広いことが必要であるが、現実には経済効率の面から
の制約があり、可能なかぎり吐出孔間隔を短縮する必要
があり、鋭意研究した結果、本発明に到達したものであ
る。
The number of each straight line group is two or more and four or more in order to secure a sufficient number of ejection holes as necessary. Further, the crossing angle of each straight line group is most preferably vertical, but it may be a diagonal crossing in the range of vertical ± 45 ° C. Further, the reason why the ejection holes are alternately arranged in a staggered manner on the intersections formed by the respective straight line groups is to avoid single yarn interference due to yarn deflection. Yarn shake occurs because the balance between the horizontal force generated by the wind flow of the cooling wind and the vertical force caused by being pulled downward is lost, and the yarn shake in the front-back direction and the yarn passing through the air at high speed In order to avoid single yarn interference that causes actual damage such as yarn unevenness and yarn breakage trouble, the left and right yarn shakes are generated by the cooling air flow acting on the air flow caused by the generated air resistance. , It is necessary that the space between adjacent discharge holes on the front, back, left, and right is wide enough, but in reality, there is a constraint from the viewpoint of economic efficiency, and it is necessary to shorten the discharge hole space as much as possible. The present invention has been reached.

【0011】すなわち、千鳥状に交互配列することによ
って、実質的な吐出孔間隔は左右方向で2c、前後方向
で2dに拡大することが可能になり、千鳥状に交互配列
しないで2cおよび2dの吐出孔間隔を維持した場合に
比べて吐出孔配置密度を大幅に高めることが可能になっ
たのである。
That is, by staggering the staggered arrangement, the substantial discharge hole interval can be expanded to 2c in the left-right direction and 2d in the front-rear direction, and 2c and 2d without staggered arrangement. As a result, the discharge hole arrangement density can be significantly increased as compared with the case where the discharge hole interval is maintained.

【0012】次に糸条を形成するブロック数が2〜4個
であり、各ブロックの吐出孔数が12〜100個である
のは、同一口金から多糸条を同時紡糸する際に、口金へ
流入する溶融ポリマーが口金の中心部と外周部で生じる
温度差や熱分解の差で粘度差を生じるため、吐出量のバ
ラツキが生じブロック数が多くなるほど糸条間のデニー
ル差が拡大するためブロック数は2〜4個でなければな
らない。また、吐出孔数が12未満の場合には本発明の
口金ではなく、従来技術の口金であっても対応可能であ
り、他方、100個以上の場合には本発明の対応が困難
になるため、吐出孔数が12〜100個でなければなら
ないのである。他方、図2の比較例の場合には、チムニ
ー冷却風の吹き抜けが困難であり、冷却風の吹出し側の
単糸のみがより強く冷却され、冷却風の吹出し側と反対
側の単糸は冷却不充分になり、単糸間で糸質差を生じる
とともにチムニー冷却風が糸条の外周部と中央の分離帯
にそって吹き抜けるため、各糸条の外周部の単糸が不規
則な糸ゆれを生じて隣接する単糸と接触するいわゆる単
糸干渉による断糸トラブルを生じるため、最少の吐出孔
間距離を単糸デニ―ルが3d以上の糸種では9mm以
上、単糸デニールが5d以上の糸種では10mm以上、
単糸デニールが10d以上の糸種では15mm以上確保
する必要があり、本発明の口金と同等の吐出孔配置密度
となすことが実質的に困難である。
Next, the number of blocks forming the yarn is 2 to 4, and the number of discharge holes in each block is 12 to 100. This means that when spinning multiple yarns simultaneously from the same spinneret. Since the molten polymer flowing into the die causes a viscosity difference due to the temperature difference and the thermal decomposition difference between the center part and the outer peripheral part of the die, the denier difference between yarns increases as the number of blocks increases as the discharge amount varies. The number of blocks must be 2-4. Further, when the number of discharge holes is less than 12, it is possible to cope with the conventional art die instead of the die of the present invention. On the other hand, when it is 100 or more, the present invention becomes difficult to deal with. The number of discharge holes must be 12 to 100. On the other hand, in the case of the comparative example of FIG. 2, it is difficult to blow through the chimney cooling air, only the single yarn on the blowing side of the cooling air is cooled more strongly, and the single yarn on the side opposite to the blowing side of the cooling air is cooled. Insufficiently causes a difference in yarn quality between single yarns, and the chimney cooling air blows out along the outer peripheral portion of the yarn and the central separation zone, so that the single yarns on the outer peripheral portion of each yarn are irregular. Causes a so-called single yarn interference that causes contact with an adjacent single yarn, and thus the minimum distance between discharge holes is 9 mm or more for a yarn type with a single yarn denier of 3 d or more, and a single yarn denier of 5 d or more. 10 mm or more for
For a yarn type having a single yarn denier of 10 d or more, it is necessary to secure 15 mm or more, and it is practically difficult to achieve a discharge hole arrangement density equivalent to that of the die of the present invention.

【0013】本発明の溶融紡糸口金は1孔当りの吐出量
が0.2g/分であるような超細単糸デニールのマルチ
フィラメントから4.0g/分であるような太単糸デニ
ールのマルチフィラメントまで極めて広い範囲の糸種群
で紡糸速度1000〜8000m/分の広い領域に渡っ
て良好に適用することができる。また本発明の吐出孔配
列は円形断面だけでなく、非円形断面孔(T孔、Y孔、
PENTA LOBAL、OCTA LOBAL、扁平
孔、中空孔、等)の吐出孔にも、良好に適用することが
できる。また、本発明の吐出孔配列は円形の多糸条同時
紡糸口金だけでなく、円形の1口金単糸条紡糸口金およ
び、非円形(正方形、長方形、楕円形)の単糸条および
多糸条同時紡糸口金にも良好に適用することができる。
本発明の溶融紡糸口金はポリエステル、ポリアミド、ポ
リプロピレン、ポリエチレン、およびこれらのポリマー
をベースとする各種共重合ポリマーや改質ポリマー等の
熱可塑性ポリマーの溶融紡糸口金として極めて良好に適
用することができる。
The melt-spinning spinneret of the present invention comprises a multifilament having a single filament denier of 4.0 g / min to a multifilament having a fine denier of 4.0 g / min and a discharge rate of 0.2 g / min per hole. It can be applied satisfactorily over a wide range of spinning speeds of 1000 to 8000 m / min with a very wide range of yarn types up to filaments. Further, the discharge hole array of the present invention is not limited to a circular cross section, but also has a non-circular cross section hole (T hole, Y hole,
PENTA LOBAL, OCTA LOBAL, flat holes, hollow holes, etc.) can also be applied favorably. Further, the discharge hole arrangement of the present invention is not limited to a circular multi-thread simultaneous spinning spinneret, but is also a circular single-spindle single-spindle spinneret and non-circular (square, rectangular, oval) single-thread and multi-thread. It can be well applied to a simultaneous spinneret.
The melt spinneret of the present invention can be applied very well as a melt spinneret of thermoplastic polymers such as polyester, polyamide, polypropylene, polyethylene, and various copolymers and modified polymers based on these polymers.

【0014】[0014]

【実施例】以下、本発明を実施例によりさらに具体的に
説明する。
EXAMPLES The present invention will be described in more detail below with reference to examples.

【0015】実施例1 図1に示すような直径a=100mm、の円形の2糸条
同時紡糸口金において、各ブロックの分離帯の間隔b=
10mm、分離帯に平行な繰り返し周期c=5mmの8
本の直線群と該直線群に直交する繰り返し周期d=5m
mの15本の直線群によって形成される交点上に千鳥状
に各ブロック48個直円形吐出孔(孔径0.23mm、
L/D=2)を交互配列した紡糸口金を作製した。ま
た、比較のために図2に示すような従来型の同心円等配
列2糸条紡糸口金(a=100mm、b=10mm、最
小孔間距離7.5mm、孔径0.23mm、L/D=
2)および、図3に示すような従来型の直線配列2糸条
同時紡糸口金(a=100mm、b=10mm、c=7
mm、d=7mm、孔径0.23mm、L/D=2)を
製作した。
Example 1 In a circular two-thread simultaneous spinning spinneret having a diameter a = 100 mm as shown in FIG.
10 mm, 8 with a repetition period c = 5 mm parallel to the separation band
Book straight line group and repetition period d = 5 m orthogonal to the straight line group
48 blocks of each block in a staggered manner on the intersection formed by a group of 15 straight lines of m (hole diameter 0.23 mm,
A spinneret in which L / D = 2) was alternately arranged was produced. For comparison, as shown in FIG. 2, a conventional type concentric circular array 2 yarn spinneret (a = 100 mm, b = 10 mm, minimum hole distance 7.5 mm, hole diameter 0.23 mm, L / D =
2) and a conventional linear array two-thread simultaneous spinneret (a = 100 mm, b = 10 mm, c = 7) as shown in FIG.
mm, d = 7 mm, hole diameter 0.23 mm, L / D = 2).

【0016】これらの紡糸口金を使用して、固有粘度
0.65で酸化チタン含有量が0.025重量%のポリ
エステルチップを紡糸温度295℃で溶融紡糸し、冷却
後2糸条に糸分けして0.6%の紡糸油剤を付与し、紡
速3250w/分で巻き取り50D−48f、100D
−48f、150D−48f、250D−48f、35
0D−48f、および450D−48fのマルチフィラ
メントを得た。このときの冷却は片面横吹きの冷却用チ
ニームを用い、図1、図2および図3の矢印の方向から
冷却風を吹き付けるように口金を取り付け、口金下10
cmから120cmの間で吹出し風速15〜35m/s
ec、温度21℃のチムニー冷却風により冷却した。こ
のとき得られたマルチフィラメントの糸斑および紡糸時
の糸切れを表1、表2および表3に示す。
Using these spinnerets, polyester chips having an intrinsic viscosity of 0.65 and a titanium oxide content of 0.025% by weight are melt-spun at a spinning temperature of 295 ° C., and after cooling, divided into two yarns. And apply 0.6% of spinning oil, and take up 50D-48f, 100D at a spinning speed of 3250 w / min.
-48f, 150D-48f, 250D-48f, 35
Multifilaments of 0D-48f and 450D-48f were obtained. For cooling at this time, a single sided cooling chinim for cooling is used, and a mouthpiece is attached so that cooling air is blown from the direction of the arrow in FIGS.
Wind speed of 15 to 35 m / s between cm and 120 cm
It was cooled with a chimney cooling air having a temperature of 21 ° C. Tables 1, 2 and 3 show the yarn unevenness of the multifilaments obtained at this time and the yarn breakage during spinning.

【0017】[0017]

【表1】 [Table 1]

【表2】 [Table 2]

【表3】 実験No.1〜6は図1に示した本発明の千鳥交互配列
口金を用いて単糸デニール1d〜9dまでのポリエステ
ル糸種を溶融紡糸した際の断糸回数と糸斑を示したもの
であるがいずれの糸種に関しても断糸発生はほとんどな
く糸斑も良好であった。一方、表2の実験No7〜12
は比較例として図2示した従来型の同心円等配列口金を
用いて、単糸デニール1d〜9dまでのポリエステル糸
種を溶融紡糸した際の断糸回数と糸斑を示したものであ
るがいずれの糸種に関しても、単糸干渉に起因する断糸
トラブルが多発するとともに、紡糸時溶融吐出ポリマー
が冷却固化する過程での糸ゆれレベルに対応した糸斑の
発生があり、工業的生産レベルにはとても達し得ないも
のであった。他方、表3の実験No.13〜18は、比
較例として図3に示した従来型の直線配列口金を用い
て、単糸デニール1d〜9dまでのポリエステル糸種を
溶融紡糸した際の断糸回数と糸斑を示したものであるが
いずれの糸種に関しても、比較例としての上記表2(実
験NO.7〜12)に比べるとやや改善した結果ではあ
ったが、本発明の口金を用いた前記表1(実験No.1
〜6)に比べて、断糸回数および糸斑ともにはるかに劣
るもであり、工業生産用としては、到底採用しえないも
のであった。
[Table 3] Experiment No. 1 to 6 show the number of yarn breakages and yarn unevenness when melt-spun polyester yarn types of single yarn denier 1d to 9d using the staggered alternate arrangement spinneret of the present invention shown in FIG. As for the yarn type, there was almost no occurrence of yarn breakage and the yarn unevenness was good. On the other hand, Experiment Nos. 7 to 12 in Table 2
As a comparative example, using the conventional concentric circular array spinneret shown in FIG. 2, the number of yarn breakages and yarn unevenness when melt-spun polyester yarn types of single yarn denier 1d to 9d are shown. Regarding yarn types, there are many yarn breakage problems due to single yarn interference, and yarn unevenness corresponding to the yarn wobbling level occurs during the process of cooling and solidification of the melt-discharging polymer during spinning. It was unattainable. On the other hand, the experiment No. 13-18 show the number of yarn breakages and yarn unevenness when melt-spun polyester yarn types of single yarn denier 1d-9d using the conventional linear array spinneret shown in FIG. 3 as a comparative example. However, for all the yarn types, the results are slightly improved as compared with Table 2 (Experiment No. 7 to 12) as a comparative example, but Table 1 (Experiment No. 7) using the spinneret of the present invention was used. 1
The number of yarn breakages and the yarn unevenness are far inferior to those of (6) to (6), and they could not be adopted at all for industrial production.

【0018】[0018]

【発明の効果】以上説明した通り、本発明の紡糸口金に
よれば、単糸デニールが0.5dレベルの細単糸デニー
ル多フィラメント糸条から、単糸デニール20dレベル
の太単糸、デニール寡フィラメント糸までの幅広い糸種
を同一口金で2〜4糸条同時紡糸により、安定した操業
性で良好な品質を維持しながら生産することが可能にな
るという効果を有する。
As described above, according to the spinneret of the present invention, the fine single yarn denier multifilament yarn having a single yarn denier of 0.5d level is changed to the single yarn denier 20d level of the thick single yarn and the denier yarn. A wide range of yarn types up to filament yarns can be produced by simultaneous spinning of 2 to 4 yarns with the same spinneret while maintaining stable operability and maintaining good quality.

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

【図1】本発明の実施例を示す2糸条同時紡糸口金の吐
出孔配置図の1例である。
FIG. 1 is an example of a discharge hole layout of a two-thread simultaneous spinning spinneret showing an embodiment of the present invention.

【図2】従来の同心円等配列2糸条同時紡糸口金の吐出
孔配置図の1例である。
FIG. 2 is an example of a discharge hole arrangement diagram of a conventional two-fiber simultaneous spinning spinneret with concentric circles and the like.

【図3】従来の直線配列2糸条同時紡糸口金の吐出孔配
置図の1例である。
FIG. 3 is an example of a discharge hole arrangement drawing of a conventional linear array two yarn simultaneous spinning spinneret.

【符号の説明】[Explanation of symbols]

1:紡糸口金 2:吐出孔 3:チムニー冷却風の吹出し方向 1: Spinneret 2: Discharge hole 3: Chimney cooling air blowing direction

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】直径ammの円形の紡糸口金に吐出孔をブ
ロック配列し、各ブロックの間隔がbmmである多糸条
同時紡糸口金において、吐出孔が繰り返し周期cmmで
平行な2本以上の直線群と該直線群に交叉する繰り返周
期dmmで、4本以上の平行な直線群によって形成され
る交点上に千鳥状に交互配列され、かつ下記条件を満た
していることを特徴とする溶融紡糸口金。 (1) 70≦a≦140 (2) 8≦b≦35 (3) 5≦c≦10 (4) 3≦d≦10 (5) 2≦ブロック数≦4 (6) 12≦各ブロックの吐出孔数≦100
1. In a multi-spindle simultaneous spinneret in which discharge holes are arranged in a block in a circular spinneret having a diameter of amm, and the intervals between the blocks are bmm, the discharge holes are two or more straight lines with a repeating cycle of cmm. Melt spinning, characterized in that they are alternately arranged in a zigzag pattern on the intersections formed by four or more parallel straight lines with a repeating cycle dmm intersecting the groups and the straight lines, and that the following conditions are met: Mouthpiece. (1) 70 ≤ a ≤ 140 (2) 8 ≤ b ≤ 35 (3) 5 ≤ c ≤ 10 (4) 3 ≤ d ≤ 10 (5) 2 ≤ number of blocks ≤ 4 (6) 12 ≤ discharge of each block Number of holes ≤100
JP5273993A 1993-11-02 1993-11-02 Spinneret for melt spinning Pending JPH07126911A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5273993A JPH07126911A (en) 1993-11-02 1993-11-02 Spinneret for melt spinning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5273993A JPH07126911A (en) 1993-11-02 1993-11-02 Spinneret for melt spinning

Publications (1)

Publication Number Publication Date
JPH07126911A true JPH07126911A (en) 1995-05-16

Family

ID=17535455

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5273993A Pending JPH07126911A (en) 1993-11-02 1993-11-02 Spinneret for melt spinning

Country Status (1)

Country Link
JP (1) JPH07126911A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
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

Cited By (2)

* Cited by examiner, † Cited by third party
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

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