JPS5988907A - Apparatus for melt spinning - Google Patents

Apparatus for melt spinning

Info

Publication number
JPS5988907A
JPS5988907A JP19605982A JP19605982A JPS5988907A JP S5988907 A JPS5988907 A JP S5988907A JP 19605982 A JP19605982 A JP 19605982A JP 19605982 A JP19605982 A JP 19605982A JP S5988907 A JPS5988907 A JP S5988907A
Authority
JP
Japan
Prior art keywords
spinning
yarn
spacer
spinneret
pack
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
Application number
JP19605982A
Other languages
Japanese (ja)
Other versions
JPS622041B2 (en
Inventor
Masahiro Matsui
正宏 松井
Kikuo Hori
堀 紀久雄
Masayuki Yamagata
正幸 山縣
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.)
Teijin Ltd
Original Assignee
Teijin Ltd
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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP19605982A priority Critical patent/JPS5988907A/en
Publication of JPS5988907A publication Critical patent/JPS5988907A/en
Publication of JPS622041B2 publication Critical patent/JPS622041B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

PURPOSE:An apparatus capable of improving the condition of spinning process and obtainng fibers of good characteristics such as strength and elongation by boring gas discharge holes in a spinning block and inseting a spacer having a passage hole for extruded filaments in delayed quenching zone with a prescribed space left below the undersurface of a spinning pack. CONSTITUTION:An apparatus equipped with a spacer 17 having a passage hole for extruded filaments 16 in close vicinity thereto in a delayed quenching zone 19 to cover the delayed quenching zone 19 with a space (d) of 3-20mm. length left below the undersurface of a spinning pack 2 and furthermore gas discharge holes 7, 6 and 10 in a spinning block 1, the pack 2 and a frame 9 respectively to discharge a hot atmosphere staying just under the spinning pack 2 above the spinning block 1. The above-mentioned apparatus permits the atmosphere just under the surface of a spinneret 18 to be discharged upward and downward in two directions.

Description

【発明の詳細な説明】 本発明は旨分子瓜会体の浴融紡糸に於て、紡糸工程調子
不調の主因である紡糸口金のノズル周囲に堆積する異物
の発生、成長を抑制し、紡糸工程調子を向上せしめると
共に、糸斑が少なく、強伸度特性の良好な繊維を製造す
る溶融紡糸装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention suppresses the generation and growth of foreign matter that accumulates around the nozzle of the spinneret, which is the main cause of poor performance in the spinning process, in bath-melt spinning of medicinal melon bodies, thereby improving the spinning process. The present invention relates to a melt spinning device that improves the tension, produces fibers with less yarn unevenness, and has good strength and elongation characteristics.

一般妬、昼分子重せ体の溶融紡糸に於ては、溶融ポリマ
ーの吐出と同時に低分子wJ質等の異物が発生し、これ
が紡糸口金面のノズル周囲に堆積し、紡糸、延伸調子や
糸質を悪化させるため、定期的に口金面に堆積した異物
なヘラ等を使用して除去したり、あるいは紡糸口金を交
換したりすることが行われているが、このためのコスト
−人件費、ポリマー−ス1機会損失等−はかなりの額と
なり、紡糸口金面の清掃や紡糸口金の交換頻度を少しで
も手減少させることは繊維製造技術者にとって古くから
の重要な課題であった。
Generally speaking, in the melt-spinning of multilayer polymers, foreign substances such as low-molecular weight substances are generated at the same time as the molten polymer is discharged, and these foreign substances accumulate around the nozzle on the spinneret surface and affect the spinning, drawing condition, and yarn. To prevent quality deterioration, foreign matter accumulated on the spinneret surface is periodically removed using a spatula or the like, or the spinneret is replaced, but the cost for this - labor costs, The loss of opportunity for polymer production is considerable, and reducing the frequency of cleaning the spinneret surface and replacing the spinneret has long been an important issue for textile manufacturing engineers.

従来から紡糸口金のノズル周囲に堆積する異物を抑制す
るために各種の方法が提案されているが、異物の成分と
しては昇華性のものが主体である事から、口金面直下の
昇華物な多量に含んだ雰囲気を系外に排出することによ
り、口金面堆積異物の発生、成長の抑制がvJ’能なこ
とが知られている。口金面直下の雰囲気を効果的に排出
する装置として、紡糸パックの下面やその上部に位置す
るスピンブロック等にこれらを貫通する排気孔を設げ、
この排気孔を介して煙突現象を利用してスピンブロック
の上方に排気スる様にしたものが提案されている(実公
昭52−8 8 1 5  )  。
Various methods have been proposed to suppress the accumulation of foreign matter around the spinneret nozzle, but since the foreign matter is mainly sublimable, a large amount of sublimated matter directly under the spinneret surface has been proposed. It is known that generation and growth of foreign matter deposited on the mouthpiece surface can be suppressed by discharging the atmosphere contained in the vJ' to the outside of the system. As a device to effectively exhaust the atmosphere directly below the spinneret surface, an exhaust hole is provided that penetrates the bottom surface of the spinning pack and the spin block located above it.
A system has been proposed in which exhaust air is passed above the spin block through this exhaust hole by utilizing the chimney phenomenon (Japanese Utility Model Publication No. 52-88-15).

しかるに、本装置では煙突効果による排気であるため、
排気量は小さく口金面堆積異物の抑制効果は充分とはい
えない。排気量を増やすため忙排気孔から強制吸引した
り、排気孔を巨大なものとすると、口金面直下に乱れを
生せしめることとなり、糸斑が悪化する。又、口金面直
下の雰囲気の排気量が多くなると口金面直下の温度が低
下するため、得られる繊維の強伸度が低いものとなり、
この面からも好ましくない。
However, with this device, the exhaust is due to the chimney effect, so
The displacement is small and the effect of suppressing foreign matter deposited on the mouthpiece surface cannot be said to be sufficient. If you force suction through a busy exhaust hole or make the exhaust hole huge in order to increase the displacement, it will cause turbulence directly below the mouthpiece surface, worsening the thread unevenness. In addition, as the amount of exhaust air directly under the nozzle surface increases, the temperature immediately below the nozzle surface decreases, resulting in lower strength and elongation of the resulting fibers.
It is not preferable from this point of view as well.

従来方法では、口金面堆積異物の抑制、即ち紡糸工程調
子の向上と糸斑、強伸度特性の向上とを両立させること
が困難であった。
In the conventional method, it has been difficult to suppress foreign matter deposited on the spinneret surface, that is, to improve the quality of the spinning process, and to improve yarn unevenness and strength and elongation properties at the same time.

本発明者らは、口金面堆積異物を減少せしめ、紡糸工程
調子を向上せしめると共に、糸斑、強伸度特性の良好な
繊維を得るべく鋭意検討した結果、本発明に到達したも
のである。
The present inventors have arrived at the present invention as a result of intensive studies aimed at reducing the amount of foreign matter deposited on the spinneret surface, improving the quality of the spinning process, and obtaining fibers with good yarn unevenness and strength and elongation properties.

すなわち、本発明は紡糸バック、遅延冷却部および冷却
風吹出面を有する強制冷却部を上から順に配置した溶融
紡糸装置において、紡糸バック直下に位置する気体をス
ピンブロック上方に排出する排気孔をスピンブロック又
はスピンブロックと紡糸パックに設けるとともに遅延冷
却部に紡出糸条と近接する糸条通路孔な有するスペーサ
を遅延冷却部を塞ぐ叩く紡糸パンク下面から下方3〜2
ommの空間を残して配設したことを特徴とするもので
ある。
That is, the present invention provides a melt spinning apparatus in which a spinning back, a delayed cooling section, and a forced cooling section having a cooling air blowing surface are arranged in order from above, and an exhaust hole for discharging gas located directly below the spinning back to the upper part of the spin block is provided in the spin block. Alternatively, a spacer provided on the spin block and the spinning pack and having a yarn passage hole adjacent to the spun yarn in the delayed cooling section is inserted 3 to 2 times downward from the bottom surface of the spinning puncture to block the delayed cooling section.
It is characterized in that it is arranged with a space of .omm left.

以下、本発明を図面に基づいて説明する。第1図は本発
明の具体例を示す概略斜視図、第2図はIIIvfr面
図である。
Hereinafter, the present invention will be explained based on the drawings. FIG. 1 is a schematic perspective view showing a specific example of the present invention, and FIG. 2 is a IIIvfr side view.

図において、lはスピンブロックで該スピンブロックl
には下部に紡糸パック2が組み込まれ、上部圧は計量ポ
ンプ3が装置されている。
In the figure, l is a spin block and the spin block l
A spinning pack 2 is installed in the lower part of the machine, and a metering pump 3 is installed to control the upper pressure.

バック2め下端には口金18が装着されここからポリマ
ーが糸条となって紡出される。4は計はポンプの実動軸
、5は溶融ポリマーの通路である。6は紡糸パック2に
設けられた複数個の排気用導孔であり、該導孔6に対応
してこれと連結する排出孔7がスピンブロック1に設け
られている。尚、これら孔6.7は対称的又は等間隔的
に配するのが好ましい。9はスピンブロック1の上面四
部8に嵌着した枠体で、該枠体9にはJJI’出孔7と
対応する位置に案内筒10が設けられ、紡糸バック直下
の雰囲気をスピンブロックlの上方に排出するようにさ
れている。
A spinneret 18 is attached to the lower end of the second bag, from which the polymer is spun into yarn. 4 is the actual shaft of the pump, and 5 is a passage for the molten polymer. Reference numeral 6 denotes a plurality of exhaust holes provided in the spinning pack 2, and exhaust holes 7 are provided in the spin block 1 in correspondence with and connected to the holes 6. Incidentally, these holes 6.7 are preferably arranged symmetrically or at equal intervals. Reference numeral 9 denotes a frame fitted to the top four parts 8 of the spin block 1, and the frame 9 is provided with a guide tube 10 at a position corresponding to the JJI' outlet 7 to direct the atmosphere directly below the spinning back to the spin block 1. It is designed to be discharged upward.

11は熱媒体による加熱室、12は保温袋である。13
は紡糸筒冷却風が紡糸口金面方向に紳士がるのを防止す
ると共に遅延冷却部を確保するための2分割されたシャ
ッター(必ずしも分’JjlJタイプにする必賛はない
)で、図示しない保持枠にスライドil能に支持され中
央部に糸条通過孔13aを形成している。14は糸条冷
却風を吹出す紡糸筒、15は糸条冷却冨、16は糸条で
ある。17は本発明に係るスペーサで、金属体からなり
、シャッター13と同様に前後に2分割された割体17
a、17bより構成され、紡糸パック2と糸条冷却室1
5との間に形成される遅延冷却部19に、紡出糸条(束
)11)に近接してこれを取囲むように形成された糸条
通路とし、ての中空部17Cを有し紡糸口金面の直下空
間を除いて遅延冷却部19をほぼ埋める如く配されてい
る。スペーサ】7は通常シャッター13上に載置(適宜
な手段を介して固定するようけてもよい。このような装
置において、紡糸口金18から吐出された糸条1らは口
金直下位置からスペーサ17.シャッター13等で取り
囲まれた遅延冷却部19の空間を走行して冷却室15に
至り紡糸筒14から吹出される冷却風により冷却固化さ
れる。
11 is a heating chamber using a heat medium, and 12 is a heat-retaining bag. 13
is a two-part shutter (not necessarily a ``JjlJ type'') that prevents the spinning tube cooling air from blowing in the direction of the spinneret surface and secures a delayed cooling section. It is slidably supported by the frame and has a thread passage hole 13a formed in the center. 14 is a spinning tube that blows out yarn cooling air, 15 is a yarn cooling volume, and 16 is a yarn. Reference numeral 17 denotes a spacer according to the present invention, which is made of a metal body and is divided into two parts in the front and the rear like the shutter 13.
a, 17b, a spinning pack 2 and a yarn cooling chamber 1.
The delayed cooling section 19 formed between the spun yarn (bundle) 11) has a yarn passageway formed to be close to and surround the spun yarn (bundle) 11), and has a hollow portion 17C. It is arranged so as to almost fill the delayed cooling section 19 except for the space directly below the mouthpiece surface. The spacer 7 is usually placed on the shutter 13 (it may also be fixed using an appropriate means. In such a device, the yarn 1 discharged from the spinneret 18 is placed on the spacer 17 from a position directly below the spinneret. .It travels through the space of the delayed cooling section 19 surrounded by the shutter 13 and the like, reaches the cooling chamber 15, and is cooled and solidified by the cooling air blown out from the spinning tube 14.

この場合、スペーサ17の中空部内壁面と紡糸口金18
の最外周(紡糸)孔18′との間隔eが水平面九投影し
た距離で測定し冷却に吠出而側(l、)で15mm以下
にされる。図に示す如く冷却風を一方向から供給するよ
うにした紡糸筒14を1史用するときには、糸条lらが
冷却風により冷却風吹出面から遠ざかる方向にたわむた
めスペーサ中空部17’ cの内壁面と紡糸口金田の最
外周孔18′との間隔は冷却風吹出面と反対側(42)
は30+nm以下、横方向(冷却風吹出方向と直交する
方向)(13)では20mm以下にして出来るだけ小さ
くするのが好ましい。尚、シャッター】3の糸条通過孔
13aも同様である。
In this case, the inner wall surface of the hollow part of the spacer 17 and the spinneret 18
The distance e from the outermost circumferential (spinning) hole 18' is measured as a distance projected on a horizontal plane and is set to 15 mm or less on the spouting side (l) for cooling. As shown in the figure, when the spinning tube 14 to which the cooling air is supplied from one direction is used for one cycle, the threads l and the like are bent in the direction away from the cooling air blowing surface by the cooling air, so that the inside of the spacer hollow part 17'c is bent. The distance between the wall surface and the outermost peripheral hole 18' of the spinneret is on the opposite side to the cooling air blowing surface (42).
is preferably 30+nm or less, and 20 mm or less in the lateral direction (direction perpendicular to the cooling air blowing direction) (13) to make it as small as possible. Incidentally, the same applies to the yarn passage hole 13a of shutter #3.

又、紡糸パック2の1α下位置はある程度の空間が必要
であり、その範囲は紡糸パック2とスペーサ17との間
隔dは3〜20mmが好ましく、この蔵囲を外れると排
出孔7による作用効果が弱まり本発明の効果を阻害する
傾向が生じる。
In addition, a certain amount of space is required at the position below 1α of the spinning pack 2, and the distance d between the spinning pack 2 and the spacer 17 is preferably 3 to 20 mm. This tends to weaken the effect of the present invention.

上に述べたような本発明装[Kより口金面に堆積する異
物の発生、成長が抑制される理由は次のように考えられ
る。
The reason why the generation and growth of foreign matter deposited on the mouthpiece surface is suppressed by the device of the present invention as described above is as follows.

紡糸1」金18から吐出された糸条ポリマーは自材の走
行のために周囲の空気を随伴流とじて下方に運搬する。
The yarn polymer discharged from the spun 1 gold 18 is transported downward by cutting off the surrounding air as an accompanying flow in order to run its own material.

口金面下の空間がかなり広い従来の紡糸装置の場合には
随伴流によって排気される空気は糸条走行速度の速い口
金面下方のものばかりであり、肝心の口金面直下位置で
は糸条走行速度が遅いため充分な随伴流が発生せず随伴
流による排気効果は殆んどない。
In the case of conventional spinning devices, which have a fairly wide space under the spinneret surface, the air exhausted by the accompanying flow is mostly below the spinneret surface where the yarn running speed is high, and at the critical position directly below the spinneret surface, the yarn running speed is low. Since the flow rate is slow, sufficient accompanying flow is not generated and the accompanying flow has almost no exhaust effect.

しかるに、本発明の如く紡糸パック2と紡糸筒14との
間にスペーサ17を設け、この間の空間が実質的に糸条
走行空間のみであると、口金面下方の糸条走行速度の速
い領域で主体的に発生する糸条随伴流が、口金面直下の
雰囲気をも吸引する形で系外へ排出可能となる。
However, if the spacer 17 is provided between the spinning pack 2 and the spinning tube 14 as in the present invention, and the space between them is essentially only a yarn running space, the problem occurs in the region below the spinneret surface where the yarn running speed is high. The yarn accompanying flow that is generated independently can be discharged to the outside of the system while also sucking the atmosphere directly below the mouth surface.

しかしながら、口金面直下の雰囲気は高温であるため下
方へ排出する能力には一定゛の限界があることは避けさ
れない。このとぎ紡糸パック2の下面とスペーサ17の
間に適度な間隙があり、しかも紡糸パック2の下面から
゛スピンブロックlを貫通してスピンブロック1の上方
に至る排気孔が設置されていると、糸条随伴流は、スペ
ーサ1上面の空気を主体的に排出するため、口金面直下
−〇雰囲気は紡糸バック1下面に沼ってまず横方向に拡
散し、一部排気孔(6,7゜10)からスピンブロック
1の上方へ排気され他はスペーサ上面を沼って、糸条随
伴流により口金面)方へ排気される。
However, since the atmosphere directly below the mouth surface is at a high temperature, it is inevitable that there is a certain limit to the ability to discharge downward. If there is an appropriate gap between the bottom surface of the spinning pack 2 and the spacer 17, and if an exhaust hole is installed from the bottom surface of the spinning pack 2 to the top of the spin block 1 through the spin block 1, Since the yarn accompanying flow mainly exhausts the air on the upper surface of the spacer 1, the atmosphere directly below the spinneret surface becomes swamped on the lower surface of the spinning back 1 and first diffuses laterally, and some exhaust holes (6, 7 degrees 10) is exhausted to the upper side of the spin block 1, and the rest is swamped on the upper surface of the spacer and is exhausted toward the spinneret surface by the yarn accompanying flow.

即ち、口金面下で空気の流れが形成され、しかも一部は
スピンブロック上方へ、一部は紡条筒方向へど2方向へ
の排気が行われるため、排気効果は著り、 <拡大され
、口金面異物堆積は飛kid的に抑制される。
In other words, an air flow is formed under the spinneret surface, and some of it is exhausted in two directions, one above the spin block and the other toward the spinning tube, so the exhaust effect is significant. , the accumulation of foreign matter on the mouthpiece surface is effectively suppressed.

本効果は、排気孔の設置と、スペーサの設置とを夫々単
J!I+に行った場合Vこは得られぬ極めて大きなもの
でル、り画期的な口金面下雰囲気排気手段といえる。
This effect can be achieved by simply installing the exhaust hole and installing the spacer! If you go to I+, V is extremely large, so it can be said to be an innovative means of exhausting the atmosphere under the face of the mouthpiece.

」こ記の説明から明らかな様に、本効果を得るためには
、スペーサの内壁面と糸条束との間隔は狭い程好ましく
、この適正距離は前記の通り、冷却風吹出面11111
で15mm以下にするのがよい。
” As is clear from this explanation, in order to obtain this effect, it is preferable that the distance between the inner wall surface of the spacer and the yarn bundle be as narrow as possible, and as described above, this appropriate distance is
It is better to make it 15mm or less.

又、紡糸バックF面とスペーサ上端面とは適度な間隔が
存在している事が必要であり、実験結果によると前述し
たように3 mm以上、20mm以・下が適正である。
Further, it is necessary that there be an appropriate distance between the spinning back F surface and the upper end surface of the spacer, and according to the experimental results, as described above, a distance of 3 mm or more and 20 mm or less is appropriate.

更に不鈍明では、糸斑に関し最も重要な、口金面直ドの
ポリマーが流動状態にある領域で、糸条随伴流により気
流が整流化されること、及び口金面下に糸条走行空間以
外の不要な空間がないためこの部分での紡糸筒冷却風の
吠上げ等による雰囲気の乱れがない事により糸斑が減少
する効果す゛ある。
Furthermore, in the area where the polymer is in a fluid state directly on the mouthpiece surface, which is the most important area for yarn unevenness, the air flow is rectified by the yarn accompanying flow, and there is no space other than the thread running space under the mouthpiece surface. Since there is no unnecessary space, there is no disturbance of the atmosphere in this area due to the howling of the spinning tube cooling wind, etc., which has the effect of reducing yarn unevenness.

更に、一般に口金面下の雰囲気を排気すると口金面下界
囲気温度が低下し、繊維の強伸度が低下するが、本発明
では口金面”Fの吐出ポリマーや、バック、スビンブ1
コック等からの熱放射のある高温雰囲気中にスペーサー
を設置するため、スペーサーが高fjAVc加熱さ第1
1、その輻射熱効果等によりこの間で糸条が保温され、
繊維の強伸度は低下せず、むしろ向上する。
Furthermore, generally when the atmosphere under the mouth surface is exhausted, the ambient temperature under the mouth surface decreases, and the strength and elongation of the fibers decreases, but in the present invention, the discharged polymer on the mouth surface "F", back,
Because the spacer is installed in a high-temperature atmosphere with heat radiation from a cock, etc., the spacer is heated to a high fjAVc.
1. The yarn is kept warm during this period due to its radiant heat effect, etc.
The strength and elongation of the fibers does not decrease, but rather improves.

以上詳述した如(、本発明装置は、紡糸口金のノスル周
囲に堆積する異物の発生、成長を太1」に抑制し、紡糸
工程調子なツ撹躍的に向上せしめると共に、糸斑2強伸
度特性の良好な繊維を作る装置1:Lをj是供するもの
であり、特に従来相反現象とされていた紡糸口金面堆積
異物の抑+fillと、糸斑、強伸度特性の向上という
両者を満足させた点で画期的な浴融紡糸装置といえる。
As described in detail above, the apparatus of the present invention suppresses the generation and growth of foreign matter that accumulates around the nostle of the spinneret to a level of 1", dramatically improves the quality of the spinning process, and improves yarn unevenness of 2 or more. This device provides equipment 1 for producing fibers with good elasticity properties, and in particular, it satisfies both the suppression of foreign matter deposited on the spinneret surface, which was considered to be a contradictory phenomenon in the past, and the improvement of yarn unevenness and strength and elongation properties. It can be said that this is a revolutionary bath melt spinning device.

次に本発明の効果を更に具体的に説明するため実施例を
示す。
Next, examples will be shown to further specifically explain the effects of the present invention.

実施例1 第1〜2図で示す冷却風が一方向から吹出される紡糸筒
を有する紡糸装置を使用し、IuM粘度(0−クロロフ
ェノール中35℃で測定)カ0.635のポリエチレン
テレフタレートを紡糸速度xzoom/分にて溶融紡糸
し50デニール/36フイラメントの糸条(但し延伸後
に測定したもの)を得た。この場合、排気孔(導孔6、
排出孔7.案内筒10)およびスペーサの南無、紡糸バ
ック下面とスペーサ上面との間隔dを変更して紡糸テス
トを行った。その結果を第1表に示す。
Example 1 Polyethylene terephthalate having an IuM viscosity (measured at 35°C in 0-chlorophenol) of 0.635 was prepared using a spinning device having a spinning tube from which cooling air was blown from one direction as shown in Figures 1 and 2. Melt spinning was performed at a spinning speed of x zoom/min to obtain a yarn of 50 denier/36 filaments (measured after stretching). In this case, the exhaust hole (guiding hole 6,
Discharge hole7. A spinning test was conducted by changing the guide cylinder 10), the size of the spacer, and the distance d between the lower surface of the spinning bag and the upper surface of the spacer. The results are shown in Table 1.

尚、iA延冷却部の黄さは100++nu、冷却風量−
兇一 は4m’/分である。
In addition, the yellowness of the iA extended cooling section is 100++nu, and the cooling air volume is -
兇一 is 4m'/min.

第1表 8は比較例である。Table 1 8 is a comparative example.

この時、スペーサの内壁面と紡糸1」釡i1に外周孔(
ピッチ円50肥)との水平距離lン冷却風吹出面側(l
、)で1’Omm、反対側(l、)で25mm、横方向
(l、)で15n+mとLだ。ココテ、紡糸上程調子は
紡糸断糸が8時間に2回以上発生するとIJ合金面清帰
することと1−1平均の口金1川/#掃周」υJ(単位
二日)で表わす。又、糸物性は延伸糸で測定したもので
あり、染斑は5点法で肉1!It刈定し、3.5点以上
が合格レベルであるが、商い点はど好ましい。
At this time, the inner wall surface of the spacer and the outer peripheral hole (
Pitch circle: 50 cm) and horizontal distance l from the cooling air outlet side (l
,) is 1'Omm, the opposite side (l,) is 25mm, and the horizontal direction (l,) is 15n+m. The quality of the spinning process is expressed by the fact that if yarn breakage occurs twice or more in 8 hours, the IJ alloy surface will be cleaned, and 1-1 average spinneret 1 stream/# sweeping'' υJ (unit: 2 days). In addition, the yarn physical properties were measured using a drawn yarn, and the dyeing spots were 1! according to the 5-point method. A score of 3.5 or higher is considered a passing level, but a trade mark is preferable.

u %はo、r%以下が合格レベルであるが低い程好ま
しい。
A pass level for u% is o, r% or less, but the lower the value, the more preferable it is.

以上の結果より、リド気孔とスペーサとの組合せにより
、夫・ン単独で紡糸した場合に比べ危局的に紡糸工程調
子が向上し、又糸品質も向上していZ)ことがわかる。
From the above results, it can be seen that the combination of the lid pores and the spacer significantly improves the spinning process condition and improves the yarn quality compared to the case of spinning alone.

夾JA′lj +9142 実施例1と全く同一条件で溶融紡糸を実施しlこ 。夾JA′lj +9142 Melt spinning was carried out under exactly the same conditions as in Example 1.

世1−スペーザの形状を種々変更上、スペーサ上面と紡
糸口金は外周孔との間隙l、、 J2. J。
World 1 - Due to various changes in the shape of the spacer, the gap between the upper surface of the spacer and the spinneret and the outer peripheral hole is 1, J2. J.

を変化せしめた。changed.

その結果を第2表に示す。The results are shown in Table 2.

第 2 衣 「 「 ト − 「 (注) 水準2.6は実施例、水準1.  J、  4
. 5は比較例である。この時、スペーサの上端面とi
tキバック下面との間隙dは1(1mmでk)った。
2nd Clothes ``To'' (Note) Level 2.6 is an example, Level 1.J, 4
.. 5 is a comparative example. At this time, the upper end surface of the spacer and i
The gap d between the t-back and the lower surface was 1 (k = 1 mm).

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

第1図は本発明の具体例を示す概略斜視図。 第2図は第1図の縦断110図である。 l・ スビソブロック 2・・・紡糸バック6・・刊気
Ill棉孔 7・・・排出孔 10・・・案内筒1:(
・・・シャッター 14・・・紡糸筒]5・冷却部 1
6・・・糸条 17・・・スペーサ1B・・・紡糸口金
 19・・・遅延冷却部′Xl  圀
FIG. 1 is a schematic perspective view showing a specific example of the present invention. FIG. 2 is a longitudinal section 110 of FIG. 1. l.Subiso block 2...Spinning bag 6...Kanki Ill cotton hole 7...Discharge hole 10...Guide cylinder 1: (
... Shutter 14 ... Spinning cylinder] 5. Cooling section 1
6... Yarn 17... Spacer 1B... Spinneret 19... Delayed cooling section 'Xl'

Claims (1)

【特許請求の範囲】[Claims] 紡糸パック、遅延冷却部および冷却風吹出面を41する
強制冷却部を上からj@に配置した溶融紡糸装置におい
て、紡糸バンク直下に位置する気体をスピンブロックの
上方に排出する排気孔をスピンブロック又はスピンブロ
ックと紡糸パックに設けるとともに遅延冷却部に紡出糸
条と近接する糸条通路孔を有するスペーサを遅延冷却l
fBを塞ぐ如く紡糸バック下面から下方3〜20mmの
空間を残して配設したことを特徴とする溶融紡糸装置。
In a melt-spinning apparatus in which a spinning pack, a delayed cooling section, and a forced cooling section with a cooling air blowing surface are arranged from above, an exhaust hole for discharging the gas located directly below the spinning bank above the spin block is connected to the spin block or A spacer provided in the spin block and the spinning pack and having a yarn passage hole adjacent to the spun yarn in the delayed cooling section is used for delayed cooling.
A melt spinning apparatus characterized in that a space of 3 to 20 mm below the bottom surface of a spinning back is left so as to close fB.
JP19605982A 1982-11-10 1982-11-10 Apparatus for melt spinning Granted JPS5988907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19605982A JPS5988907A (en) 1982-11-10 1982-11-10 Apparatus for melt spinning

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19605982A JPS5988907A (en) 1982-11-10 1982-11-10 Apparatus for melt spinning

Publications (2)

Publication Number Publication Date
JPS5988907A true JPS5988907A (en) 1984-05-23
JPS622041B2 JPS622041B2 (en) 1987-01-17

Family

ID=16351510

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19605982A Granted JPS5988907A (en) 1982-11-10 1982-11-10 Apparatus for melt spinning

Country Status (1)

Country Link
JP (1) JPS5988907A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4877107A (en) * 1972-01-25 1973-10-17
JPS528815U (en) * 1975-07-04 1977-01-21
JPS5761710A (en) * 1980-09-25 1982-04-14 Teijin Ltd Melt spinning apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4877107A (en) * 1972-01-25 1973-10-17
JPS528815U (en) * 1975-07-04 1977-01-21
JPS5761710A (en) * 1980-09-25 1982-04-14 Teijin Ltd Melt spinning apparatus

Also Published As

Publication number Publication date
JPS622041B2 (en) 1987-01-17

Similar Documents

Publication Publication Date Title
KR0177261B1 (en) Process and device for producing cellulose fibres
JP4968378B2 (en) Spinning pack for dry and wet spinning, and fiber bundle manufacturing equipment
JP6558288B2 (en) Method for producing acrylonitrile fiber bundle and method for producing carbon fiber bundle
US20050220916A1 (en) Spinning device and method having turbulent cooling by blowing
RU2132418C1 (en) Forming apparatus
JPH0217641B2 (en)
JP2010106393A (en) Apparatus and method for producing multifilament yarn
JP2000503076A (en) Method and apparatus for producing melt spun monofilament
BR0011173B1 (en) melt spinning apparatus and process for spinning continuous polymeric filaments.
JP4187368B2 (en) Pressurized steam treatment apparatus and method for yarn
JPS59228012A (en) Wet spinning process
JP3483070B2 (en) Wet spinning device
JPS5988907A (en) Apparatus for melt spinning
JP6504088B2 (en) Method of manufacturing acrylonitrile-based fiber bundle
KR950007807B1 (en) Process for preparing polyester filamentary meterial
JP3554659B2 (en) Spinning device for ultra-fine multifilament yarn
JP2002038328A (en) Apparatus for melt spinning
JPS5976912A (en) Melt spinning apparatus
JP2003193325A (en) Melt spinning equipment
KR100305668B1 (en) Multifilament Quenching Apparatus
JPS63767Y2 (en)
JPS6146563B2 (en)
TW201839192A (en) Method for manufacturing acrylonitrile based fiber bundle and method for manufacturing carbon fiber bundle
JP5332253B2 (en) Filament yarn manufacturing apparatus and manufacturing method
JP3658915B2 (en) High speed melt spinning equipment