JPH03193948A - Production of self-elongating polyester filament yarn - Google Patents

Production of self-elongating polyester filament yarn

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Publication number
JPH03193948A
JPH03193948A JP33200089A JP33200089A JPH03193948A JP H03193948 A JPH03193948 A JP H03193948A JP 33200089 A JP33200089 A JP 33200089A JP 33200089 A JP33200089 A JP 33200089A JP H03193948 A JPH03193948 A JP H03193948A
Authority
JP
Japan
Prior art keywords
yarn
heat treatment
filament yarn
temperature
polyester filament
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
JP33200089A
Other languages
Japanese (ja)
Other versions
JP2884649B2 (en
Inventor
Toshihiko Kimura
俊彦 木村
Rumi Karasawa
留美 柄澤
Masao Miyake
三宅 昌男
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 JP33200089A priority Critical patent/JP2884649B2/en
Publication of JPH03193948A publication Critical patent/JPH03193948A/en
Application granted granted Critical
Publication of JP2884649B2 publication Critical patent/JP2884649B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To obtain the title yarn having improved self-elongation ratio, coloring properties in dyeing, fastness, soft handle, etc., readily manifesting bulkiness, by treating undrawn highly orientated polyester yarn by dry heat and then drawing and heat-treating under a specific condition. CONSTITUTION:Undrawn highly orientated polyester filament yarn having 20-90X10<-3> n double refraction is heated by dry heating under <=0.05g/g low tension at 125-145 deg.C preferably while subjecting the yarn to air interlacing treatment. Then, the resulting yarn is drawn and heat-treated at >=Tg of the undrawn highly orientated polyester yarn (preferably 100-110 deg.C) at >=1.3 draw ratio to give the objective filament yarn.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、湿熱でフリー収縮処理後、フリー乾熱処理を
施すことによって、自発伸長するポリエステルフィラメ
ント糸の製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing polyester filament yarn that spontaneously stretches by performing a free dry heat treatment after a free shrinkage treatment with wet heat.

[従来技術] 従来、自発伸長するポリエステルフィラメント糸の製造
方法として、例えば、特公昭63−46167号公報に
記載されている如く、ポリエステルフィラメント糸を2
次転移点以上110℃以下の温度で熱延伸し、さらに2
次転移点以下の低温で延伸して潜在的自発伸長性ポリエ
ステルフィラメント糸を得る方法が提案されている。
[Prior Art] Conventionally, as a method for producing spontaneously elongating polyester filament yarn, for example, as described in Japanese Patent Publication No. 63-46167, polyester filament yarn is
Next, hot stretching is carried out at a temperature above the transition point and below 110°C, and further 2
A method of obtaining a potentially spontaneously extensible polyester filament yarn by drawing at a low temperature below the next transition temperature has been proposed.

[発明が解決しようとする課題] しかしながら、かかる方法によって得られる糸は、比較
的高い結晶度を生じない条件下で熱処理を施しているの
で、室温や経時変化の影響を受けやすくなり、伸長斑が
起こりやすくなったり、また染色加工した後の染色ケン
ロウ性が低下するなど、品位の低下をもたらすものであ
った。
[Problems to be Solved by the Invention] However, since the yarn obtained by this method is heat-treated under conditions that do not produce a relatively high degree of crystallinity, it becomes susceptible to changes in room temperature and over time, resulting in uneven elongation. This caused deterioration in quality, such as increased likelihood of oxidation occurring and a decrease in dyeing strength after dyeing.

また、高温染色では脆化が激しく編織物の引き裂き強力
が低下する問題があった。
In addition, high-temperature dyeing causes severe embrittlement and reduces the tear strength of the knitted fabric.

本発明の目的は、上記したような点に鑑み、比較的高い
結晶度を生じる条件下で熱延伸加工を繰り返し、上記し
た品位の低下を改善し、かつ発色性向上と風合のソフト
化をはかる自発伸長するポリエステルフィラメント糸の
製造方法を提供せんとするものである。
In view of the above-mentioned points, the object of the present invention is to improve the above-mentioned deterioration of quality, improve color development, and soften texture by repeating hot stretching under conditions that produce relatively high crystallinity. It is an object of the present invention to provide a method for producing a polyester filament yarn that stretches spontaneously.

[課題を解決するための手段] 上記した目的を達成する本発明の自発伸長ポリエステル
フィラメント糸の製造方法は、以下の構成からなる。
[Means for Solving the Problems] The method for producing spontaneously elongated polyester filament yarn of the present invention, which achieves the above-mentioned objects, has the following configuration.

すなわち、複屈折率Δnが20〜90X10′3の範囲
にあるポリエステル高配向未延伸糸を、0゜05g/d
以下の低張力下、125〜145℃の温度範囲で乾熱処
理を行い、次いで該ポリエステル高配向未延伸糸の7g
以上の温度にて1.3倍以上の延伸熱処理を施すことを
特徴とする自発伸長ポリエステルフィラメント糸の製造
方法である。
That is, a polyester highly oriented undrawn yarn having a birefringence Δn in the range of 20 to 90×10′3 was heated at 0°05 g/d.
Dry heat treatment is performed in a temperature range of 125 to 145°C under the following low tension, and then 7g of the highly oriented undrawn polyester yarn
This is a method for producing a spontaneously elongated polyester filament yarn, which is characterized by carrying out a stretching heat treatment of 1.3 times or more at the above temperature.

上記の方法によって得られる延伸熱処理後のポリエステ
ルフィラメント糸は、延伸熱処理後、湿熱でフリー収縮
させた後、150℃以上でフリー乾熱処理を施すことに
よって、自発伸張する糸となる。
The polyester filament yarn after the drawing heat treatment obtained by the above method is subjected to free shrinkage with moist heat after the drawing heat treatment, and then subjected to a free dry heat treatment at 150° C. or higher to become a yarn that stretches spontaneously.

なお、低張力乾熱処理を施す際には、空気交絡処理を施
しつつ行なうことが好ましい。
Note that when performing the low tension dry heat treatment, it is preferable to perform the air entanglement treatment.

以下、さらに詳しく本発明について説明をする。The present invention will be explained in more detail below.

本発明は、例えば、紡糸速度1500〜450Qm/m
inで高速紡糸して得られた複屈折率Δnが20〜90
X10′Bの範囲にあるポリエステル高配向未延伸糸を
用いる。
The present invention, for example, has a spinning speed of 1500 to 450 Qm/m.
The birefringence Δn obtained by high-speed spinning in is 20 to 90
A highly oriented undrawn polyester yarn in the range of X10'B is used.

複屈折率Δnが20X10−3より小さい場合は、該未
延伸糸の構造が不安定であるため、室温や経時変化の影
響を受けやすくなり自発伸長斑を起こしたり、糸加工性
が不安定になりやすい。また染色加工した場合染色ケン
ロウ性が低くなり、安定した品質を供給することはでき
ない。
If the birefringence Δn is smaller than 20X10-3, the structure of the undrawn yarn is unstable, so it becomes susceptible to room temperature and changes over time, causing spontaneous elongation unevenness and unstable yarn processability. Prone. Furthermore, when dyed, the dyeing strength becomes low and stable quality cannot be supplied.

一方、Δnが90X10”を越えると、既に繊維内部で
結晶化が進んでいるので、沸騰水で収縮させた後の収縮
率は極めて低いものであり、また150℃以上の乾熱処
理後に起こる自発伸長の能力はほとんど無くなる。
On the other hand, if Δn exceeds 90x10'', crystallization has already progressed inside the fiber, so the shrinkage rate after shrinking with boiling water is extremely low, and spontaneous elongation occurs after dry heat treatment at 150°C or higher. ability is almost lost.

次いで、本発明方法は前記のポリエステル高配向未延伸
糸を用いて125〜145℃の温度で乾熱処理する。乾
熱処理の温度が125℃より低いと、後述するが、湿熱
でフリー収縮させた後の収縮率が大きくなり過ぎるため
、染色時の収縮が大き過ぎて、一般の衣料加工には適さ
ない。また、乾熱処理の温度が145℃を越えると、乾
熱処理温度が高すぎて、糸の脆化が激しくなり、低延伸
張力下では糸の加工が極めて難しい。この場合の延伸張
力は0.05g/d以下とするものである。
Next, in the method of the present invention, the highly oriented undrawn polyester yarn described above is subjected to a dry heat treatment at a temperature of 125 to 145°C. If the temperature of the dry heat treatment is lower than 125° C., as will be described later, the shrinkage rate after free shrinkage with wet heat becomes too large, and the shrinkage during dyeing becomes too large, making it unsuitable for general clothing processing. Furthermore, if the dry heat treatment temperature exceeds 145° C., the dry heat treatment temperature is too high and the yarn becomes brittle, making it extremely difficult to process the yarn under low drawing tension. The stretching tension in this case is 0.05 g/d or less.

延伸張力はなるべく低いほど好ましいが、強度の低下や
脆化が大きくなるので加工性を充分考慮する必要がある
Although it is preferable that the stretching tension be as low as possible, sufficient consideration must be given to workability, since this increases the reduction in strength and embrittlement.

加工性の低下を改善する方法としては、乾熱処理中に例
えばインターレースノズルを用いて空気交絡処理を施す
ことが効果的である。空気交絡処理は、フィラメント糸
に集束性および丸みを与え、その時、交絡がかかること
によって糸の長さ方向に縮みが生じるので、長さが吸収
され、延伸張力を大幅に下げて糸加工することができる
。つまり延伸倍率を下げることができる。ただし、空気
交絡処理の圧力が高い場合や、流量が多い場合は、イラ
ツキ斑になりやすいので適宜条件を選ぶことが好ましい
。空気交絡処理の圧力は、一般には、3kg/a1以下
が適している。また、空気交絡処理のノズルはインター
レース用あるいは乱流用のいずれであってもよいが、イ
ンターレース用の方が加工性やコストの点で好ましい。
As a method for improving the deterioration of processability, it is effective to perform air entanglement treatment using, for example, an interlace nozzle during the dry heat treatment. The air entanglement process gives the filament yarn cohesiveness and roundness, and at that time, the entanglement causes shrinkage in the length direction of the yarn, so the length is absorbed and the yarn can be processed by significantly lowering the drawing tension. I can do it. In other words, the stretching ratio can be lowered. However, if the pressure of the air entanglement treatment is high or if the flow rate is large, it is easy to cause uneven spots, so it is preferable to select the conditions appropriately. Generally, a pressure of 3 kg/a1 or less is suitable for the air entanglement treatment. Further, the nozzle for the air entanglement treatment may be either for interlacing or for turbulent flow, but the nozzle for interlacing is preferable in terms of workability and cost.

なお、延伸張力が0.05g/d以下となる延伸倍率は
ζ約1゜1〜1.5倍相当になる。
Note that the stretching ratio at which the stretching tension is 0.05 g/d or less is equivalent to approximately ζ1°1 to 1.5 times.

このようにして、低張力乾熱処理したフィラメント糸は
2次転移点つまり、7g以上の温度で1゜3倍以上の延
伸熱処理を施すのである。延伸温度は7g以上の温度と
するものであるが、100〜110℃の温度範囲が適し
ている。
In this way, the filament yarn subjected to the low tension dry heat treatment is subjected to a drawing heat treatment of 1.3 times or more at a temperature of 7 g or more, which is the secondary transition point. The stretching temperature is set to 7 g or more, but a temperature range of 100 to 110°C is suitable.

延伸温度がTgより低いと、湿熱処理後の収縮率が高く
なり過ぎることや、繊維内部の構造が不安定になるので
好ましくない。
If the stretching temperature is lower than Tg, it is not preferable because the shrinkage rate after wet heat treatment becomes too high and the internal structure of the fiber becomes unstable.

なお、延伸温度が130℃以上の高温度では、結晶化お
よび配向が進み自発伸長の発現が低下するので、好まし
くない。
Note that a stretching temperature as high as 130° C. or higher is not preferable because crystallization and orientation progress and the spontaneous elongation is reduced.

この様にして、特殊な条件で延伸熱処理を繰り返したポ
リエステルフィラメント糸は潜在的に自発伸長の能力を
持つことになる。
In this way, polyester filament yarns that have been repeatedly subjected to drawing heat treatment under special conditions potentially have the ability to spontaneously elongate.

該フィラメント糸を沸騰水でフリー収縮させた後の収縮
率は通常のポリエステルフィラメント糸並の値を有する
10〜20%の範囲にある。なお、沸騰水は98℃以上
の高圧下における高温水であってもよい。
The shrinkage rate of the filament yarn after free shrinkage in boiling water is in the range of 10 to 20%, which is comparable to ordinary polyester filament yarn. Note that the boiling water may be high-temperature water under high pressure of 98° C. or higher.

続いて該フィラメント糸を150℃以上において、フリ
ー乾熱処理を施すことによって通常のポリエステルフィ
ラメント糸では、さらに収縮が進み、3〜10%は収縮
するが、本発明の自発伸長ポリエステルフィラメント糸
では逆に1%以上の伸長を示すものである。つまり自発
伸長するのである。伸長率は延伸熱処理によっては5〜
10%の高いもとなる。
Subsequently, by subjecting the filament yarn to a free dry heat treatment at 150°C or higher, ordinary polyester filament yarns undergo further shrinkage, shrinking by 3 to 10%, but with the spontaneously elongated polyester filament yarns of the present invention, on the contrary. This shows an elongation of 1% or more. In other words, it grows spontaneously. The elongation rate varies from 5 to 5 depending on the stretching heat treatment.
The cost is as high as 10%.

この性質を利用したものとして、編織物の風合い改善例
がある。例えば、染色仕上げ加工においてリラックスさ
せ、染色工程で充分収縮処理を行い、しかる後に仕上げ
加工で乾熱”処理を行なうことによって、−旦緻密にな
った構造を緩め、布帛に曲げやすさや嵩をもたらして柔
らかさを与えることができるのである。
An example of using this property is to improve the texture of knitted fabrics. For example, by relaxing the fabric during the finishing process, applying sufficient shrinkage during the dyeing process, and then applying dry heat treatment during the finishing process, the previously dense structure is loosened and the fabric becomes more flexible and bulky. It can give softness.

本発明の製造方法を図面に示す実施例に基づいてさらに
説明するならば、第1図は、本発明に係る自発伸長ポリ
エステルフィラメント糸の製造工程を示す一実施例図で
ある。
To further explain the manufacturing method of the present invention based on an example shown in the drawings, FIG. 1 is an example diagram showing the manufacturing process of a spontaneously elongated polyester filament yarn according to the present invention.

第1図において、ポリエステル高配向未延伸糸1を巻糸
体から解舒し、ガイド2からフィードローラ3へ供給し
、フィードローラ6との間の第1ヒータ5で乾熱処理を
施す。該乾熱処理を低張力下で処理するために、延伸倍
率を下げる目的として空気交絡処理のノズル4を用いて
もよい。続いてフィードローラ6とデリベリ−ローラ8
との間の第2ヒータ7で延伸熱処理を施した後、巻き取
りローラ9によってチーズに巻き上げる。
In FIG. 1, a highly oriented undrawn polyester yarn 1 is unwound from a spool, fed from a guide 2 to a feed roller 3, and subjected to dry heat treatment by a first heater 5 between it and the feed roller 6. In order to carry out the dry heat treatment under low tension, an air entanglement treatment nozzle 4 may be used for the purpose of lowering the stretching ratio. Next, feed roller 6 and delivery roller 8
After being subjected to a stretching heat treatment with a second heater 7 between the two, the cheese is rolled up into cheese by a winding roller 9.

実施例1 紡糸速度3500m/minで高速紡糸して得られた複
屈折率Δnが46.2X10′3のポリエステル高配向
未延伸糸75デニール、36フイラメント糸を温度13
0℃、1.2g (0,016g/d)の張力下(1,
25倍の延伸倍率)で乾熱処理を施し、次いで、110
℃で1.5倍の延伸倍率で熱処理を施し、自発伸長性能
を有するフィラメント糸を製造した。
Example 1 Highly oriented undrawn polyester yarn with a birefringence Δn of 46.2×10'3 obtained by high-speed spinning at a spinning speed of 3500 m/min, 75 denier, 36 filament yarn was heated at a temperature of 13
0℃, under tension of 1.2g (0,016g/d) (1,
Dry heat treatment was performed at a stretching ratio of 25 times, and then 110 times
A filament yarn having spontaneous elongation performance was produced by heat treatment at a draw ratio of 1.5 times at °C.

得られたフィラメント糸を沸騰水(98℃)でフリー収
縮させた後の収縮率は15.6%であった。さらに18
0℃のフリー乾熱処理を施すことによって13.3%の
収縮率を得た。つまり2゜3%(15,3−13,3)
の自発伸長率を有した。
The shrinkage rate of the obtained filament yarn after free shrinkage in boiling water (98° C.) was 15.6%. 18 more
A shrinkage rate of 13.3% was obtained by performing free dry heat treatment at 0°C. That is 2°3% (15,3-13,3)
It had a spontaneous elongation rate of .

実施例2 同じく、紡糸速度3500m/minで高速紡糸して得
られた複屈折率Δnが46.2X10”のポリエステル
高配向未延伸糸75デニール、36フイラメント糸を温
度140℃、0.7gの張力下(1,15倍の延伸倍率
)で、圧空圧2Kg/dの空気交絡処理を行いつつ乾熱
処理を施し、次いで、110℃で1.5倍の延伸倍率で
熱処理を施し、自発伸長性能を有するポリエステルフィ
ラメント糸を製造した。
Example 2 Similarly, a highly oriented undrawn polyester yarn of 75 denier and 36 filament yarn with a birefringence index Δn of 46.2×10” obtained by high-speed spinning at a spinning speed of 3500 m/min was spun at a temperature of 140° C. and a tension of 0.7 g. Dry heat treatment was performed while performing air entanglement treatment at a compressed air pressure of 2 Kg/d at a stretching ratio of 1.5 times (stretching ratio of 1.15 times), and then heat treatment was performed at a stretching ratio of 1.5 times at 110°C to evaluate spontaneous elongation performance. A polyester filament yarn having the following properties was produced.

同様に、該フィラメント糸を沸騰水でフリー収縮させた
後の収縮率は18.2%であり、さらに180℃のフリ
ー乾熱処理を施すことによって12.5%の収縮率を得
た。つまり5.7%(18゜2−12.5)の自発伸長
率を有した。
Similarly, the shrinkage rate of the filament yarn after free shrinking with boiling water was 18.2%, and by further subjecting it to free dry heat treatment at 180°C, a shrinkage rate of 12.5% was obtained. In other words, it had a spontaneous elongation rate of 5.7% (18°2-12.5).

実施例3 紡糸速度3500m/minで高速紡糸して得られた複
屈折率Δnが46.2X10′3のポリエステル高配向
未延伸糸75デニール、36フイラメント糸を温度80
〜160℃、張力0.7〜1゜8g下(延伸倍率は1.
1倍)で低張力乾熱延伸を行ない、次いで、温度110
℃で1.5倍の延伸熱処理を行ない自発伸張性能を有す
るポリエステルフィラメント糸を得た。乾熱処理温度と
自発伸長率の関係を第2図に示した。
Example 3 A highly oriented undrawn polyester yarn of 75 denier and 36 filament yarn with a birefringence Δn of 46.2×10'3 obtained by high-speed spinning at a spinning speed of 3500 m/min was heated at a temperature of 80 m/min.
~160°C, tension 0.7~1°8g (stretching ratio is 1.
low tension dry heat stretching at a temperature of 110
A polyester filament yarn having spontaneous elongation performance was obtained by carrying out a heat treatment for stretching 1.5 times at ℃. Figure 2 shows the relationship between dry heat treatment temperature and spontaneous elongation rate.

熱処理温度が125℃以上になると自発伸長が発生し1
35℃付近でピークを示し140℃以上になると自発伸
長が停止する。
When the heat treatment temperature exceeds 125℃, spontaneous elongation occurs and 1
It shows a peak around 35°C, and spontaneous elongation stops when the temperature reaches 140°C or higher.

よって、上記の条件によって得られる自発伸張ポリエス
テルフィラメント糸の自発伸張が発生する熱処理温度は
125〜140℃である。
Therefore, the heat treatment temperature at which spontaneous elongation of the spontaneously elongated polyester filament yarn obtained under the above conditions occurs is 125 to 140°C.

なお、第2図においては、フィラメント糸を沸騰水で収
縮させた後の収縮率81.さらに180℃の乾熱処理し
た後の収縮率S2とし、自発伸長率は31−32として
求めた。ここで、31−82が正(+)になれば自発伸
長しており、負(−)になれば自発伸長していないこと
である。
In addition, in FIG. 2, the shrinkage rate after shrinking the filament yarn with boiling water is 81. Further, the shrinkage rate after dry heat treatment at 180°C was determined as S2, and the spontaneous elongation rate was determined as 31-32. Here, if 31-82 is positive (+), spontaneous expansion is occurring, and if it is negative (-), spontaneous expansion is not occurring.

実施例4 紡糸速度3500m/minで高速紡糸して得られた複
屈折率Δnが46.2X10′3のポリエステル高配向
未延伸糸75デニール、36フイラメント糸を温度13
0℃で0.9gの張力下(1゜25倍の延伸倍率)で低
張力乾熱熱処理を施し、1.5倍の延伸倍率で延伸熱処
理を施した。延伸熱処理温度と沸騰水で収縮させた後の
収縮率の関係を第3図に示した。
Example 4 A highly oriented undrawn polyester yarn of 75 denier and 36 filament yarn with a birefringence Δn of 46.2×10'3 obtained by high-speed spinning at a spinning speed of 3500 m/min was heated at a temperature of 13
A low tension dry heat treatment was performed at 0° C. under a tension of 0.9 g (1°, 25 times the stretching ratio), and a stretching heat treatment was performed at a stretching ratio of 1.5 times. Figure 3 shows the relationship between the stretching heat treatment temperature and the shrinkage rate after shrinkage with boiling water.

延伸熱処理温度が80℃以上、つまりポリエステル高配
向未延伸糸のTg温度以上になれば収縮率は大幅に低下
し衣料用として好′ましい範囲になる。
If the drawing heat treatment temperature is 80° C. or higher, that is, the Tg temperature of the highly oriented undrawn polyester yarn, the shrinkage rate will be significantly reduced and fall within a preferable range for clothing.

通常、収縮率は20%以下でないと風合が硬くなるので
好ましくないので、延伸熱処理温度はTg温度以上とす
るのがよい。また、120℃以上では配向・結晶化が進
み収縮率が低下すると共に、自発伸長能力も低下するの
で好ましくない。
Generally, if the shrinkage rate is not 20% or less, the texture becomes hard, which is not preferable, so the stretching heat treatment temperature is preferably set to Tg temperature or higher. Further, if the temperature is 120° C. or higher, orientation and crystallization will proceed and the shrinkage rate will decrease, as well as the spontaneous elongation ability will decrease, which is not preferable.

[発明の効果] 本発明は、上記の構成とすることにより、次の如き優れ
た効果を奏する。
[Effects of the Invention] With the above configuration, the present invention provides the following excellent effects.

すなわち、自発伸長を有するポリエステルフィラメント
糸を編織物とし、染色のリラックスで充分収縮を起こさ
せると収縮率は20%以下と通常の延伸ポリエステルフ
ィラメント重亜になるので、風合が特別硬(なることは
ない。
In other words, if a polyester filament yarn with spontaneous elongation is made into a knitted fabric and sufficiently shrunk by relaxing dyeing, the shrinkage rate will be 20% or less, making it a normal drawn polyester filament yarn, so the texture will be particularly hard. There isn't.

染色後、仕上げセットを行うことにより、一端収縮した
該ポリエステル糸が伸びるので組織の拘束力が緩み、風
合はソフトになり嵩がでやすい。
After dyeing, finishing setting is performed to stretch the polyester yarn, which has shrunk at one end, thereby loosening the binding force of the structure, making the texture soft and bulky.

特に、収縮差のあるフィラメント糸を組み合わせると、
例えば、芯部に本発明糸を用い、鞘部に本発明糸より収
縮率の低いフィラメント糸を用いることにより、高密度
で柔らかい風合の編織物が得られる。
In particular, when combining filament yarns with differential shrinkage,
For example, by using the yarn of the present invention in the core portion and the filament yarn having a lower shrinkage rate than the yarn of the present invention in the sheath portion, a knitted fabric with high density and a soft texture can be obtained.

また、鞘部に本発明糸を芯部に用い、本発明糸より収縮
率の高いフィラメント糸を用いることにより、高密度で
嵩ばりの有る風合が得られる。
Further, by using the yarn of the present invention in the core portion of the sheath portion and using filament yarn with a higher shrinkage rate than the yarn of the present invention, a texture with high density and bulk can be obtained.

乾熱処理温度は、7g以上であることから、高い結晶度
でセットされており、室温の影響や経日変化を受けるこ
とが少ない。
Since the dry heat treatment temperature is 7 g or more, it is set at a high degree of crystallinity, and is less affected by room temperature and changes over time.

さらに、125〜140℃でセットされていることから
、染色における発色性やケンロウ性は高い。
Furthermore, since the temperature is set at 125 to 140°C, the color development and brightness in dyeing are high.

空気交絡処理を行ないつつ熱処理を施すことによって、
該フィラメント糸に集束性および丸みを与え、その時、
交絡がかかることによって糸の長さ方向に縮みが生じる
ので、長さが吸収され延伸張力をかなり下げて糸加工す
ることができる。つまり延伸倍率を下げることができる
。そのため、本発明の効果である、自発伸長率や染色に
おける発色性、ケンロウ性等の効果が向上したり、風合
がソフトに成る。
By applying heat treatment while performing air entanglement treatment,
imparting cohesiveness and roundness to the filament yarn;
Since the yarn shrinks in the longitudinal direction due to entanglement, the length is absorbed and the yarn can be processed with considerably lower stretching tension. In other words, the stretching ratio can be lowered. Therefore, the effects of the present invention, such as spontaneous elongation rate, color development in dyeing, and waxiness, are improved, and the texture is soft.

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

第1図は、本発明に係る自発伸長ポリエステルフィラメ
ント糸の製造工程を示す一実施例図である。第2図は、
熱処理温度と自発伸長率の関係を示すグラフである。第
3図は、延伸熱処理温度と沸騰水で収縮させた後の収縮
率の関係を示すグラフである。 1:ポリエステル高配向未延伸糸 2ニガイド 3:フィードローラ 4:空気交絡ノズル 5:第1ヒータ 6:フィードローラ 7:第2ヒータ 8:デリベリ−ローラ 9:巻取ローラ
FIG. 1 is an example diagram showing the manufacturing process of a spontaneously elongated polyester filament yarn according to the present invention. Figure 2 shows
It is a graph showing the relationship between heat treatment temperature and spontaneous elongation rate. FIG. 3 is a graph showing the relationship between the stretching heat treatment temperature and the shrinkage rate after shrinkage with boiling water. 1: Polyester highly oriented undrawn yarn 2 guide 3: Feed roller 4: Air entangling nozzle 5: First heater 6: Feed roller 7: Second heater 8: Delivery roller 9: Take-up roller

Claims (2)

【特許請求の範囲】[Claims] (1)複屈折率Δnが20〜90×10^−^3の範囲
にあるポリエステル高配向未延伸糸を、0.05g/d
以下の低張力下、125〜145℃の温度範囲で乾熱処
理を行い、次いで該ポリエステル高配向未延伸糸のTg
以上の温度にて1.3倍以上の延伸熱処理を施すことを
特徴とする自発伸長ポリエステルフィラメント糸の製造
方法。
(1) Highly oriented undrawn polyester yarn with a birefringence Δn in the range of 20 to 90 x 10^-^3 at 0.05 g/d
Dry heat treatment is performed in a temperature range of 125 to 145°C under the following low tension, and then the Tg of the highly oriented undrawn polyester yarn is
1. A method for producing spontaneously elongated polyester filament yarn, which comprises subjecting a stretching heat treatment to 1.3 times or more at a temperature above.
(2)空気交絡処理を施しつつ低張力乾熱処理すること
を特徴とする請求項1記載の自発伸長ポリエステルフィ
ラメント糸の製造方法。
(2) The method for producing spontaneously elongated polyester filament yarn according to claim 1, characterized in that a low tension dry heat treatment is performed while performing an air entanglement treatment.
JP33200089A 1989-12-20 1989-12-20 Method for producing spontaneously elongated polyester filament yarn Expired - Lifetime JP2884649B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33200089A JP2884649B2 (en) 1989-12-20 1989-12-20 Method for producing spontaneously elongated polyester filament yarn

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33200089A JP2884649B2 (en) 1989-12-20 1989-12-20 Method for producing spontaneously elongated polyester filament yarn

Publications (2)

Publication Number Publication Date
JPH03193948A true JPH03193948A (en) 1991-08-23
JP2884649B2 JP2884649B2 (en) 1999-04-19

Family

ID=18250021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33200089A Expired - Lifetime JP2884649B2 (en) 1989-12-20 1989-12-20 Method for producing spontaneously elongated polyester filament yarn

Country Status (1)

Country Link
JP (1) JP2884649B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100318138B1 (en) * 1994-11-24 2002-05-13 조민호 Manufacturing method of polyester salt reflection

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100318138B1 (en) * 1994-11-24 2002-05-13 조민호 Manufacturing method of polyester salt reflection

Also Published As

Publication number Publication date
JP2884649B2 (en) 1999-04-19

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