JPS636647B2 - - Google Patents
Info
- Publication number
- JPS636647B2 JPS636647B2 JP58242217A JP24221783A JPS636647B2 JP S636647 B2 JPS636647 B2 JP S636647B2 JP 58242217 A JP58242217 A JP 58242217A JP 24221783 A JP24221783 A JP 24221783A JP S636647 B2 JPS636647 B2 JP S636647B2
- Authority
- JP
- Japan
- Prior art keywords
- yarn
- roller
- godet roller
- speed
- godet
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000000034 method Methods 0.000 claims description 22
- 229920000728 polyester Polymers 0.000 claims description 12
- 238000010036 direct spinning Methods 0.000 claims description 10
- 239000000835 fiber Substances 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 3
- 238000002074 melt spinning Methods 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 description 7
- 238000009987 spinning Methods 0.000 description 6
- 238000005485 electric heating Methods 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 3
- 230000009477 glass transition Effects 0.000 description 3
- 238000009998 heat setting Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 230000003746 surface roughness Effects 0.000 description 3
- 238000004804 winding Methods 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- WSQZNZLOZXSBHA-UHFFFAOYSA-N 3,8-dioxabicyclo[8.2.2]tetradeca-1(12),10,13-triene-2,9-dione Chemical compound O=C1OCCCCOC(=O)C2=CC=C1C=C2 WSQZNZLOZXSBHA-UHFFFAOYSA-N 0.000 description 1
- LLLVZDVNHNWSDS-UHFFFAOYSA-N 4-methylidene-3,5-dioxabicyclo[5.2.2]undeca-1(9),7,10-triene-2,6-dione Chemical compound C1(C2=CC=C(C(=O)OC(=C)O1)C=C2)=O LLLVZDVNHNWSDS-UHFFFAOYSA-N 0.000 description 1
- -1 Polyethylene terephthalate Polymers 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 230000001050 lubricating effect Effects 0.000 description 1
- 238000011089 mechanical engineering Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000139 polyethylene terephthalate Polymers 0.000 description 1
- 239000005020 polyethylene terephthalate Substances 0.000 description 1
- 238000004886 process control Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Description
〔技術分野〕
本発明はポリエステル繊維をより高速で簡略な
プロセスで安価に製造する直接紡糸延伸方法に関
するものである。
〔従来技術とその欠点〕
直接紡糸延伸方法は既によく知られており、現
在では広く生産工程に採用されている。
例えば、特公昭50―3406号公報などは紡出糸条
を冷却固化後、第1ゴデツトローラで引取り、引
き続いて第2ゴデツトローラへ導いて延伸する
際、未延伸糸糸条を予備加熱して延伸する方法を
提案している。又第1ゴデツトローラを加熱する
加熱ゴデツトローラ延伸方法はよく知られてい
る。これらの法では未延伸糸を延伸する際に、ポ
リエステル未延伸糸をガラス転移温度以上に予備
加熱することにより、延伸を容易にせんとするも
のである。
一方近年では、より簡略な設備、低エネルギー
で低コストの糸をつくることが要求されている。
しかしながら、70〜90℃に加熱した第1ゴデツ
トローラを用いる法では均一延伸するために未延
伸糸の適当な加熱コントロールに多くの労を費し
た。
すなわち未延伸糸のガラス転移点付近までホツ
トローラで糸条加熱する際、油水分量、糸条の開
繊状態、ローラへの接触時間、ローラ近傍の雰囲
気温度等により糸条加熱状態が変り、工程管理面
で困難であつた。
さらに生産性の欠点として第1ゴデツトローラ
を加熱することで、該ローラ上の糸条張力は極端
に低下するために、糸ゆれは増大し糸切れを起す
欠点があつた。加えて第2ゴデツトローラ上の糸
ゆれも5000m/分付近になるとローラの回転随伴
気流の増大もあり、糸ゆれが増加し、延伸糸と言
えども糸条間の接触があると糸切れを起す欠点も
あつた。
さらに、この従来方法はホツトローラの熱源と
しては取扱いが容易であることから電熱ヒータを
用いることもあつて電熱コストが高く、設備費が
高くなり、複雑で延伸速度も5000m/分以下では
高生産性の要求に対しては満足できるものでな
く、改善の余地があつた。
これら従来の直接紡糸延伸方法の欠点を改善す
る目的で特に高速化による生産性向上をねらつた
高速紡糸方法なる提案も近年多く出されている。
例えば特開昭55―107511号公報などは紡糸速度
4500m/分以上で引取ることにより、延伸(機械
倍率)や熱セツトなくして実用に耐える有用な糸
構造とするシンプルな高速製糸方法を提案してい
る。
この種の製法で得た糸質は低速で紡糸して延伸
倍率を付与して得た延伸糸糸質とは本質的に構造
を異にする特異点がある。例えば紡速6000m/分
で引取つて延伸糸とした糸の伸度は50〜60%であ
り、沸収率は2〜3%と極端に低下する独得の糸
物性を有している。
〔発明の目的〕
発明者らは延伸、巻上速度を5000m/分、
6000m/分あるいはそれ以上とする直接紡糸延伸
方法で糸物性を従来の加熱延伸による直接紡糸延
伸方法のものと類似させることに主眼を置いて簡
略な高速直接紡糸延伸方法について検討を重ねた
結果、以下に詳述する如く、新規で有益な方法を
見出したのである。
〔発明の構成〕
すなわち、本発明はポリエステルを溶融紡糸
し、冷却固化後、口金面下3m以内で糸条を集束
つつ、給油して、鏡面仕上げの非加熱第1ゴデツ
トローラで4500m/分以上で引取り、引き続き粗
度40〜70Hrms〔「機械工学便覧」第5版第17―
176〜177頁(昭和48年6月15日 日本機械学会発
行)参照〕の梨地加工を施した第2ゴデツトロー
ラへ導き、第1と第2ゴデツトローラ間で延伸す
ることを特徴とするポリエステル繊維の直接紡糸
延伸方法である。
以下本発明を図を用いて詳述する。
第1図は本発明の実施態様の1例を示す直接紡
糸延伸装置の正面概要図である。
ポリエステルを溶融して口金1より吐出させて
未延伸糸糸条2とする。冷却装置3により冷却固
化後、3m以内に設けた給油装置4により、未延
伸糸糸条を集束させながら所定の油剤を糸条に付
与する。そして、非加熱の第1ゴデツトローラ5
で4500m/分以上で引取り、引き続き表面に梨地
加工を施した第2ゴデツトローラ6に導き、第1
ゴデツトローラ5と第2ゴデツトローラ6との間
で両ローラの周速度差により延伸し、巻取機7に
よつてパツケージ8を得る。必要に応じて巻取機
の前に集束用ノズルを設けてよい。
本発明の直接紡糸延伸方法における最大の特徴
点は従来法のように第1ゴデツトローラを加熱し
ないことである。つまり、本発明では第1ゴデツ
トローラを常温(室温)とし、予備加熱しないた
めローラ上での糸条張力低下がなく、第1、第2
ゴデツトローラ上の糸ゆれが非常に少なく、この
ためローラ上の糸条間接触による糸切れが大巾に
減少し生産性が向上する。
また、引取速度を4500m/分以上とすることで
配向がある程度進み収縮率が減少してくるため、
たとえば延伸後熱セツト処理を施す場合でもその
熱セツト温度も下げられ、大巾な電熱コストを削
減することができる。
第1ゴデツトローラ5は高速回転可能なローラ
で4500m/分以上の周速度が得られれば良く、短
尺ローラで加熱ヒータは不要である。該ローラに
より未延伸糸を4500m/分以上の速度に正確に規
制して引取る必要がある。従つて、従動型あるい
は強制駆動型のセパレートローラ5′を用いて、
糸条を第1ゴデツトローラと該セパレートローラ
とに1回以上撓囲しても良く、又第1ゴデツトロ
ーラの表面を鏡面仕上げとすれば、糸条のスリツ
プがないのでセパレートローラ5′を通さないで
第1ゴデツトローラに1回以下の巻付けで引取速
度を規制することができる。
このような第1ゴデツトロール囲りの条件を採
用することで従来法の長尺加熱型第1ゴデツトロ
ーラを用いる必要もなく、巻数も少ないので非常
にコンパクトで安価な設備費とすることができ
る。加えて、第1ゴデツトローラを加熱しないの
で該ローラ上での糸ゆれは大巾に減少し高速引取
が可能になる効果がある。
本発明では、第1ゴデツトローラ5で糸条を引
取る前に口金面下3m以内で集束しつつ給油装置
4で給油する必要がある。糸条に集束を施すの
は、第1ゴデツトローラによる引取速度が
4500m/分以上におよぶことにより、糸条の随伴
気流が極端に増大して糸条張力のアツプで単糸配
向度に不均一性を生じ、断糸と糸質異常を防止す
るためである。この給油装置4は口金面に近づけ
るほど随伴気流の程度が小さくて有効であるが、
口金に近づけすぎて固化点以前に配置することは
糸切れを起し好ましくない。適正に位置としては
固化直後で、口金面下3mの範囲に配置すること
が重要である。給油装置を口金面下3m以上とす
ると、前記したように、高速で引取るために糸条
の随伴気流が加速度的に増加して、糸切れした
り、糸質が不均一になる。
集束方法は集束ガイドを兼用した給油ガイドが
最も好ましいが、給油装置直後に別のガイドを設
けて集束してもよい。
一方、本発明においては、第2ゴデツトローラ
6は表面を梨地化することが極めて重要である。
これは該ローラへの糸条巻付き防止、工程張力の
安定化のため有利である。このため、第2ゴデツ
トローラ6の表面の粗度をHrms40〜70の範囲と
するのが好ましい、Hrms70を越える場合はロー
ラ上での糸条のスベリが起り延伸斑を生じ、
Hrms40未満で糸離れが悪くなる傾向になり、さ
らに第2ゴデツトローラを鏡面仕上げにすると該
ローラへの糸条巻付きが頻発し、安定した延伸糸
が得られず操業上不利である。
所望に応じて第2梨地ゴデツトローラを加熱し
て延伸糸を熱セツトしてもよい。第2ゴデツトロ
ーラの表面を梨地化することで延伸速度の規制が
やや不安定になるので第2ゴデツトローラと対に
なつているセパレートローラ6′を用いて、この
両者ローラ上に糸条を1回以上撓囲することが望
しい。延伸速度の規制面から好ましくは3回以上
撓囲する方が良い。
本発明では、集束しつつ給油した糸条を第1ゴ
デツトローラで4500m/分以上の引取速度で引取
るのである。引取速度が4500m/分未満では糸の
構造は未延伸領域のため第1ゴデツトローラを加
熱(ガラス転移温度以上)しないで延伸するとウ
ースタ斑が増加するのである。すなわち、本発明
では引取速度4500m/分以上にして延伸前の糸条
構造をなるべく延伸糸構造に近づけんとするもの
である。
本発明のポリエステルは、エチレンテレフタレ
ートを主たる繰返し単位とするポリエステルを主
に対象とするが、ブチレンテレフタレートを繰返
し単位とするポリエステルであつてもよい。ま
た、15モル%以下の量で他の成分を1種以上共重
合したポリエステルおよび少量の添加剤を含有し
たポリエステルであつてもよい。
〔発明の効果〕
本発明においては、このように高速で紡糸引取
を行なつても、従来法と同様、糸質は第1、第2
ゴデツトローラ間で付与する延伸倍率の変更で所
望の残留伸度20〜45%の間に自由に選択でき、か
つ第2ゴデツトローラを加熱すれば収縮率も所望
のレベルに選択できるメリツトがある。
そして、本発明は非常にシンプルなプロセスで
電熱コストが低く、しかも安定した延伸糸を生産
性よく得ることができる。
以下実施例により本発明を具体的に説明する。
実施例 1
〔η〕=0.65のポリエチレンテレフタレートを
90℃で溶融し、直径0.3mmφの孔36個を有する口
金から押し出し、冷却し、糸条に油剤を1.0重量
%を付与し、次いで第1ゴデツトローラと第2ゴ
デツトローラの条件、給油位置を表―1のとおり
変更して延伸後、巻取り、75d−36フイラメント
の延伸糸を得た。該糸の糸質を表―1に示した。
なお、室温は30℃とした。また、梨地加工した第
2ゴデツトローラの表面粗度は55Hrmsとした。
[Technical Field] The present invention relates to a direct spinning/drawing method for producing polyester fibers at higher speeds, simpler processes, and at lower costs. [Prior Art and Its Disadvantages] Direct spinning and drawing methods are already well known and are now widely adopted in production processes. For example, Japanese Patent Publication No. 50-3406 discloses that after the spun yarn is cooled and solidified, it is taken up by a first godet roller and subsequently guided to a second godet roller for drawing, and the undrawn yarn is preheated and drawn. We are proposing a method to do so. Further, a heated godet roller stretching method in which the first godet roller is heated is well known. In these methods, when drawing the undrawn yarn, the undrawn polyester yarn is preheated to a temperature higher than the glass transition temperature to facilitate the drawing. On the other hand, in recent years, there has been a demand for producing threads with simpler equipment, lower energy consumption, and lower cost. However, in the method using the first godet roller heated to 70 to 90 DEG C., a lot of effort was required to properly control the heating of the undrawn yarn in order to achieve uniform drawing. In other words, when heating the yarn with a hot roller to near the glass transition point of undrawn yarn, the heating state of the yarn changes depending on the oil/water content, the opening state of the yarn, the contact time with the roller, the ambient temperature near the roller, etc., and process control is affected. It was difficult in many ways. Furthermore, as a drawback of productivity, heating the first godet roller causes the yarn tension on the roller to be extremely reduced, resulting in increased yarn wobbling and yarn breakage. In addition, when the yarn sway on the second godet roller reaches around 5000 m/min, the airflow accompanying the rotation of the roller increases, which increases yarn sway, and even if it is a drawn yarn, it can cause yarn breakage if there is contact between yarns. It was hot too. Furthermore, since this conventional method is easy to handle as a heat source for hot rollers, it also uses an electric heater, which results in high electric heating costs, high equipment costs, and is complicated and requires high productivity when the stretching speed is less than 5000 m/min. The requirements were not satisfied and there was room for improvement. In order to improve the shortcomings of these conventional direct spinning and drawing methods, many proposals have been made in recent years for high-speed spinning methods that are particularly aimed at improving productivity by increasing the speed.
For example, in JP-A No. 55-107511, the spinning speed is
We are proposing a simple high-speed spinning method that creates a useful yarn structure that can withstand practical use without drawing (mechanical magnification) or heat setting by drawing at a speed of 4,500 m/min or more. The yarn quality obtained by this type of manufacturing method has a unique point in that it is essentially different in structure from the drawn yarn quality obtained by spinning at a low speed and applying a drawing ratio. For example, the elongation of a drawn yarn drawn at a spinning speed of 6000 m/min is 50 to 60%, and the boiling yield is extremely low to 2 to 3%. [Object of the invention] The inventors set the stretching and winding speed to 5000 m/min.
As a result of repeated studies on a simple high-speed direct spinning/drawing method with a focus on making the yarn physical properties similar to those of the conventional direct spinning/drawing method using heated drawing using a direct spinning/drawing method at 6000 m/min or more, we found that We have discovered a new and advantageous method, as detailed below. [Structure of the Invention] That is, the present invention melt-spun polyester, cooled and solidified it, then focused the yarn within 3 m below the spinneret surface, oiled it, and spun it at 4500 m/min or more using a mirror-finished non-heated first godet roller. Pick up, continue roughness 40~70Hrms ["Mechanical Engineering Handbook" 5th edition No. 17]
176-177 (Published by the Japan Society of Mechanical Engineers, June 15, 1977)], the polyester fiber is guided to a second godet roller with a satin finish and stretched between the first and second godet rollers. This is a spinning and drawing method. The present invention will be explained in detail below using figures. FIG. 1 is a schematic front view of a direct spinning and drawing apparatus showing one example of an embodiment of the present invention. Polyester is melted and discharged from a spinneret 1 to form an undrawn thread 2. After being cooled and solidified by the cooling device 3, a predetermined oil agent is applied to the undrawn yarns while converging the undrawn yarns by the oil supply device 4 provided within 3 m. And the non-heated first godet roller 5
It is taken over at a speed of 4,500 m/min or more, and then guided to the second godet roller 6 whose surface has been treated with a matte finish, and then the first
It is stretched between the godet roller 5 and the second godet roller 6 due to the difference in circumferential speed between both rollers, and a package 8 is obtained by a winder 7. If necessary, a focusing nozzle may be provided before the winder. The most distinctive feature of the direct spinning and drawing method of the present invention is that the first godet roller is not heated, unlike the conventional method. That is, in the present invention, the first godet roller is kept at normal temperature (room temperature) and is not preheated, so there is no decrease in yarn tension on the roller, and the first and second godet rollers are kept at room temperature.
There is very little yarn wobbling on the godet roller, which greatly reduces yarn breakage due to contact between yarns on the roller, improving productivity. In addition, by setting the take-up speed to 4500 m/min or more, the orientation will progress to a certain extent and the shrinkage rate will decrease.
For example, even if a heat setting treatment is performed after stretching, the heat setting temperature can be lowered, making it possible to significantly reduce electric heating costs. The first godet roller 5 is a roller that can rotate at high speed and only needs to have a circumferential speed of 4500 m/min or more, and is a short roller that does not require a heater. It is necessary to accurately regulate the undrawn yarn to a speed of 4500 m/min or more and take it off using the roller. Therefore, using a driven type or forced drive type separate roller 5',
The yarn may be wrapped around the first godet roller and the separate roller one or more times, and if the surface of the first godet roller is mirror-finished, the yarn will not slip, so it will not pass through the separate roller 5'. The take-up speed can be regulated by winding the first godet roller once or less. By adopting such conditions for surrounding the first godet roller, there is no need to use the long heating type first godet roller of the conventional method, and the number of windings is small, making it possible to make the equipment very compact and inexpensive. In addition, since the first godet roller is not heated, the yarn sway on the roller is greatly reduced, making it possible to take the yarn at high speed. In the present invention, before the yarn is taken up by the first godet roller 5, it is necessary to collect the yarn within 3 m below the mouth surface and to supply oil with the oil supply device 4. The yarn is bundled by the first Godet roller's take-up speed.
This is to prevent yarn breakage and yarn quality abnormalities due to the increase in yarn tension, which causes non-uniformity in the degree of single yarn orientation due to the extremely increased airflow accompanying the yarn by increasing the speed to 4500 m/min or more. The closer the oil supply device 4 is to the mouth surface, the smaller the degree of accompanying airflow, which makes it more effective.
Placing it too close to the cap before the solidification point is undesirable as it may cause thread breakage. As for the proper location, it is important to place it immediately after solidification, within a range of 3m below the mouth surface. If the lubricating device is located 3 m or more below the mouth surface, as described above, the air flow accompanying the yarn will increase at an accelerating rate due to high-speed take-off, resulting in yarn breakage and uneven yarn quality. As for the focusing method, it is most preferable to use a refueling guide that also serves as a focusing guide, but another guide may be provided immediately after the refueling device to perform focusing. On the other hand, in the present invention, it is extremely important that the second godet roller 6 has a matte surface.
This is advantageous because it prevents the yarn from wrapping around the roller and stabilizes the tension in the process. For this reason, it is preferable that the surface roughness of the second godet roller 6 is in the range of Hrms 40 to 70. If it exceeds Hrms 70, the yarn will slip on the roller, causing stretching unevenness.
If the Hrms is less than 40, yarn separation tends to worsen, and if the second godet roller is given a mirror finish, the yarn will frequently wind around the roller, making it difficult to obtain a stable drawn yarn, which is disadvantageous in terms of operation. If desired, the drawn yarn may be heat set by heating the second satin godet roller. By making the surface of the second godet roller matte, the regulation of the drawing speed becomes somewhat unstable, so a separate roller 6' paired with the second godet roller is used to pass the yarn onto both rollers one or more times. It is desirable to be surrounded. From the viewpoint of regulating the drawing speed, it is preferable to bend the film three or more times. In the present invention, the yarn, which has been bundled and oiled, is taken off by the first godet roller at a taking-up speed of 4500 m/min or more. When the take-up speed is less than 4,500 m/min, the yarn structure is in an undrawn region, so if the first godet roller is drawn without being heated (to above the glass transition temperature), Worcester spots will increase. That is, in the present invention, the take-up speed is set to 4500 m/min or higher to make the yarn structure before drawing as close to the drawn yarn structure as possible. The polyester of the present invention is mainly a polyester having ethylene terephthalate as a main repeating unit, but may also be a polyester having butylene terephthalate as a repeating unit. It may also be a polyester copolymerized with one or more other components in an amount of 15 mol% or less, and a polyester containing a small amount of additives. [Effects of the Invention] In the present invention, even when the yarn is taken off at such a high speed, the yarn quality remains the same as in the conventional method.
It has the advantage that the desired residual elongation can be freely selected between 20 and 45% by changing the stretching ratio applied between the godet rollers, and the shrinkage rate can also be selected to a desired level by heating the second godet roller. In addition, the present invention is a very simple process with low electric heating costs and can produce stable drawn yarn with high productivity. The present invention will be specifically explained below using Examples. Example 1 Polyethylene terephthalate with [η] = 0.65
It is melted at 90℃, extruded through a nozzle with 36 holes with a diameter of 0.3 mmφ, cooled, and 1.0% by weight of lubricant is applied to the yarn.Then, the conditions of the first godet roller and the second godet roller, and the oiling position are shown. After stretching with the same changes as in 1, the yarn was wound up to obtain a drawn yarn of 75d-36 filament. The quality of the yarn is shown in Table 1.
Note that the room temperature was 30°C. In addition, the surface roughness of the second godet roller which was satin finished was 55 Hrms.
【表】
実験No.1、2、4、6、7、10および12は本発
明の効果を明確にするための比較例を示す。No.
1、2は第1ゴデツトローラを100℃、80℃に予
熱したもので糸質面では問題ないが第1ゴデツト
ローラ上の糸ゆれ大、電熱コスト、設備費が高く
満足できる方法ではない。
No.4、10は第2ゴデツトローラの表面を鏡面仕
上げにしたもので、第2ゴデツトローラから糸離
れが悪く、ローラへの巻付きが多かつた。
No.6、7は冷延伸方法であることから設備費、
電熱コスト面では改善されたが、引取速度が低い
ため糸質面、糸切れ面、生産性の面で各々欠点が
ある。
No.12は給油する位置までの距離が長く随伴気流
の増大があり、糸むら、糸切れの欠点があつた。
これらに比して実施例No.3、5、8、9および11
は前記欠点が解消された優れた効果を示してい
る。
実施例 2
第2ゴデツトローラの表面粗度を種々変更した
以外は実施例1実験No.3と同一条件で延伸糸を得
た。該糸の糸質を表―2に示した。[Table] Experiment Nos. 1, 2, 4, 6, 7, 10 and 12 show comparative examples for clarifying the effects of the present invention. No.
In methods 1 and 2, the first godet roller is preheated to 100°C and 80°C, which poses no problem in terms of yarn quality, but is not a satisfactory method because of large yarn fluctuation on the first godet roller, high electric heating cost, and high equipment cost. In Nos. 4 and 10, the surface of the second godet roller was mirror-finished, and the yarn did not easily separate from the second godet roller, and the yarn was often wrapped around the roller. No. 6 and 7 are cold stretching methods, so equipment costs,
Although the electric heating cost has been improved, there are drawbacks in terms of yarn quality, yarn breakage, and productivity due to the low take-up speed. No. 12 had a long distance to the refueling position, which caused an increase in accompanying airflow, and had the disadvantages of thread unevenness and thread breakage.
Compared to these, Example Nos. 3, 5, 8, 9 and 11
shows an excellent effect in which the above-mentioned drawbacks are eliminated. Example 2 A drawn yarn was obtained under the same conditions as in Experiment No. 3 of Example 1, except that the surface roughness of the second godet roller was variously changed. The quality of the yarn is shown in Table 2.
【表】
実験No.13および16は本発明の効果を明確にする
ための比較例である。
No.13は糸離れが悪くローラへの巻付きが多かつ
た。
No.16は延伸張力が不安定になり延伸斑が生じ安
定した延伸糸が得られなかつた。[Table] Experiments No. 13 and 16 are comparative examples for clarifying the effects of the present invention. In No. 13, the thread did not separate easily and was often wrapped around the roller. In No. 16, the drawing tension became unstable and uneven drawing occurred, making it impossible to obtain a stable drawn yarn.
第1図は本発明の実施態様の1例を示す直接紡
糸延伸装置の正面概略図である。
1:口金、2:糸条、3:冷却装置、4:給油
装置、5:第1ゴデツトローラ、5′:セパレー
トローラ、6:第2ゴデツトローラ、6′:セパ
レートローラ、7:巻取機、8:パツケージ。
FIG. 1 is a schematic front view of a direct spinning/drawing apparatus showing one example of an embodiment of the present invention. 1: Cap, 2: Yarn, 3: Cooling device, 4: Oil supply device, 5: First godet roller, 5': Separate roller, 6: Second godet roller, 6': Separate roller, 7: Winder, 8 :Package.
Claims (1)
金面下3m以内で糸条を集束しつつ、給油して鏡
面仕上げの非加熱の第1ゴデツトローラで
4500m/分以上で引取り、引き続き粗度40〜
70Hrmsの梨地加工を施した第2ゴデツトローラ
へ導き、第1、第2ゴデツトローラ間で延伸する
ことを特徴とするポリエステル繊維の直接紡糸延
伸方法。1. After melt-spinning polyester and solidifying it by cooling, the yarn is bundled within 3m below the spinneret surface while being oiled and spun using a non-heated first godet roller with a mirror finish.
Pick up at 4500m/min or more, continue roughness 40~
A method for direct spinning and drawing of polyester fibers, characterized in that the fibers are guided to a second godet roller that has been subjected to a satin finish for 70 hours, and then drawn between the first and second godet rollers.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24221783A JPS60134022A (en) | 1983-12-23 | 1983-12-23 | Direct spin-draw process for polyester fiber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP24221783A JPS60134022A (en) | 1983-12-23 | 1983-12-23 | Direct spin-draw process for polyester fiber |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60134022A JPS60134022A (en) | 1985-07-17 |
JPS636647B2 true JPS636647B2 (en) | 1988-02-10 |
Family
ID=17085981
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP24221783A Granted JPS60134022A (en) | 1983-12-23 | 1983-12-23 | Direct spin-draw process for polyester fiber |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60134022A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62162016A (en) * | 1986-01-07 | 1987-07-17 | Teijin Ltd | Production of polyester fiber |
US9732443B2 (en) | 2013-09-02 | 2017-08-15 | Tokyo Institute Of Technology | Polyester fiber |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49134915A (en) * | 1973-05-04 | 1974-12-25 | ||
JPS53143728A (en) * | 1977-05-16 | 1978-12-14 | Teijin Ltd | Production of polyester filament yarns |
-
1983
- 1983-12-23 JP JP24221783A patent/JPS60134022A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49134915A (en) * | 1973-05-04 | 1974-12-25 | ||
JPS53143728A (en) * | 1977-05-16 | 1978-12-14 | Teijin Ltd | Production of polyester filament yarns |
Also Published As
Publication number | Publication date |
---|---|
JPS60134022A (en) | 1985-07-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR860001531B1 (en) | Preparation of amorphous ultra-high-speed-spun polyethylene terephthalate yarn for texturing | |
JPS636647B2 (en) | ||
JPS5822565B2 (en) | High speed spinning method | |
WO2023087649A1 (en) | Tension heat-setting treatment device and high-modulus chinlon 66 industrial filament production method | |
EP0089912A2 (en) | Process for the production of high-strength polyester yarn | |
JPS61275420A (en) | Method for direct spinning and drawing of polyester yarn | |
JP2000256916A (en) | Method for direct spinning and drawing of polyester yarn | |
JPS61194218A (en) | Production of polyester fiber | |
JPS61160419A (en) | Production of combined filament polyester yarn having heat-shrinkage difference | |
JP2768675B2 (en) | Direct spinning and drawing method for polyester yarn | |
JPS6411724B2 (en) | ||
JPS5818445B2 (en) | Polyester fiber manufacturing method | |
JPH09175731A (en) | High speed winding method of synthetic fiber and synthetic fiber cheese-like package | |
JPS6359412A (en) | Spinning of polyester | |
JPH02229211A (en) | Production of polyester fiber | |
JPS61160417A (en) | Production of polyhexamethylene adipamide fiber | |
JPH0447045B2 (en) | ||
JPS60104516A (en) | Manufacture of polyester filament | |
JP4395977B2 (en) | Method for producing polyamide fiber | |
JPH02229212A (en) | Production of polyester fiber | |
JP2895530B2 (en) | Method for producing large fine filament yarn | |
JP2000273719A (en) | High-speed spinning of multifilament yarn of polyamide yarn | |
JPS59125904A (en) | Manufacture of polyester multifilament for separation | |
JPS5818446B2 (en) | Polyester fabric | |
JPS60231814A (en) | Preparation of multifilament for dividing |