JPS58163718A - Preparation of polyester fiber - Google Patents

Preparation of polyester fiber

Info

Publication number
JPS58163718A
JPS58163718A JP3936682A JP3936682A JPS58163718A JP S58163718 A JPS58163718 A JP S58163718A JP 3936682 A JP3936682 A JP 3936682A JP 3936682 A JP3936682 A JP 3936682A JP S58163718 A JPS58163718 A JP S58163718A
Authority
JP
Japan
Prior art keywords
polyester
fibers
particles
inert
fiber
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
JP3936682A
Other languages
Japanese (ja)
Other versions
JPS641583B2 (en
Inventor
Motoyoshi Suzuki
鈴木 東義
Masaaki Sekimoto
関本 雅章
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 JP3936682A priority Critical patent/JPS58163718A/en
Publication of JPS58163718A publication Critical patent/JPS58163718A/en
Publication of JPS641583B2 publication Critical patent/JPS641583B2/ja
Granted legal-status Critical Current

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  • Chemical Or Physical Treatment Of Fibers (AREA)
  • Artificial Filaments (AREA)

Abstract

PURPOSE:To obtain the titled fibers having special micropores and depth and brightness of color in coloring, by drawing undrawn polyester fibers, containing specific inert fine particles, and having a specific birefringence and crystallinity under unheated conditions, and eluting the resultant drawn fibers partially with an alkali. CONSTITUTION:Undrawn polyester fibers, containing 0.1-5wt% inert fine particles having <100mmu average primary particle diameter and fine inert particles having >=100mmu particle diameter in such a state that >=3 secondary aggregated particles adjacent thereto at a distance between the centers of the primary particles of less than twice of the primary particle diameter may not be present in 10mu<2> cross-sectional area by observing in an enlarged electron microscopic photograph to such an extent as to discriminate the primary particle diameter, and having 0.07-0.14 birefringence (DELTAn) of the total fibers, <=0.06 birefringence (DELTAna) in the amorphous region and >=30% crystallinity (Xc) are drawn under unheated conditions at 1.05-1.35 draw ratio, and then treated with an alkali to elute >=2wt% fibers therefrom.

Description

【発明の詳細な説明】 本慟−はポーエステル繊維の製造法に■する。[Detailed description of the invention] This article describes a method for producing poester fiber.

1[K―麿には、譬−な徽繻孔を有11着色した−に改
善された色の深みと鮮明性を呈するポリエステル繊維の
製造法に関する。
The present invention relates to a method for producing polyester fibers having improved color depth and clarity compared to K-11, which has a unique perforation and is colored.

ポ曽エステルは参(の優れた特性を有するがゆえに合成
繊維として広く使用されている。しかLながら、ポリエ
ステル繊維は羊唱や絹の如會天然繊維、レー厘ンやアセ
テートの如會繊膳**鐵艙、アタψル皐繊維等に比較し
て1着色したIINC色Kllみがないため偽色!に、
鮮明性に劣る欠点がある。
Polyester fibers are widely used as synthetic fibers due to their excellent properties. However, polyester fibers can be used as natural fibers such as silk and silk, as well as fibers such as lace and acetate. **False color because there is no IINC color Kll color compared to iron ore fibers, etc.
It has the disadvantage of poor clarity.

従来より、この欠点を解消せんとして、染料の改譬ヤポ
リエステルの化学改質等が試みやれて會だが、いずれも
元分な効果は得られていない、また、ポリエステル繊艙
表面に透−薄膜を膠或Sせる方法や繊騙物真爾Kso〜
10・諺ム・vm/−のプラX1鳳射を總して繊維表1
1に黴顔な凹凸を形成させる方法勢1)s提案さ九てい
る。
In order to overcome this drawback, attempts have been made to modify dyes and chemically modify polyester, but none of them have been effective. How to make it glue or S
10. Proverbs: VM/-'s plastic
Nine methods have been proposed for forming mold-like irregularities on the surface of the surface.

しかしながら、これらの方法によっても1色の深みを改
善する効果は不充分であり、その上繊維表面に形成され
た透明薄膜は洗潅等によって容易に脱落し、その耐久性
も不充分であり、プラズマ照射を總す方法では、照射面
の影になる織■部分の繊維の表面に!!l凸が生じない
ため、着用中に生じる繊維組織内での糸の転び等によっ
て平滑繊維面が表面にでて色斑になる欠点がある。
However, even with these methods, the effect of improving the depth of a single color is insufficient, and in addition, the transparent thin film formed on the fiber surface easily falls off when washed, etc., and its durability is insufficient. In the method that uses plasma irradiation, the surface of the fiber in the weave part that is in the shadow of the irradiated surface! ! Since no convexity occurs, there is a drawback that the smooth fiber surface is exposed to the surface due to the rolling of threads within the fiber structure during wear, resulting in color spots.

他方、ポリエステル繊維の表面に凹凸を付与する方法と
して、ポリオキシエチレングリコール又はポリオキシエ
チレングリコールとスルホン酸化合物を配合したポリエ
ステルよりなる繊―をアルカリ水溶液で処理することk
より繊維軸方向に配列した練状の微細孔を繊維表wK形
成させる吸湿性繊細の製造法、又は酸化亜鉛。
On the other hand, as a method of imparting irregularities to the surface of polyester fibers, fibers made of polyoxyethylene glycol or polyester blended with polyoxyethylene glycol and a sulfonic acid compound are treated with an aqueous alkaline solution.
A method for producing hygroscopic fine pores on the fiber surface WK, or zinc oxide, in which kneaded micropores arranged in the fiber axis direction are formed.

リン酸カルシウ五等の如き不活性無機物質の微粒子をポ
リエステル反応系内に添加配合せしめてなるポリエステ
ル繊維を、アルカリ水l1111で地理して無機黴着子
を11幽することにより微細孔を形成させる歇am繊維
の製造法等が提案されている。しかしながら、これらの
方法によって得られる繊維には1色の深みを改善する効
果は−められず、かえって1感濃度の低下が認められる
。jlち、これらの方法において、アルカリ水滴IIK
よる処lI#!充秀でないときは、色の欅みを改善す番
効果は食く■められず、またアルカ−水製Ilkよる処
理が光分なときは、色の緑°みを改善、するどころか、
微細孔による光の1厘射によるためか、視感一度が低下
し、濃色に着色しCも白つぼく1えるよ5になり、その
上置られる繊維の強直が着しく低下し、容易にフィプシ
ル化するようになり夷jlK耐、えない。
A polyester fiber prepared by adding fine particles of an inert inorganic substance such as calcium phosphate to a polyester reaction system is mixed with alkaline water to remove inorganic mold particles to form micropores. Methods for producing AM fibers have been proposed. However, the fibers obtained by these methods do not have the effect of improving the depth of one color, and on the contrary, a decrease in one-sensitivity density is observed. In these methods, alkaline water droplets IIK
#! When it is not Mitsuhide, the effect of improving the brightness of the color cannot be taken into account, and when the treatment with alkaline water Ilk is light, it does not improve the greenness of the color.
Perhaps due to the irradiation of light from the micropores, the visual sense deteriorates, the color becomes dark, and the C color becomes white (1 to 5), and the stiffness of the fibers placed on top of it deteriorates, making it easier to see. It becomes difficult to form fipsyl.

また、曽子径$・Jujターン以下のシ替力の如會無機
徽粒子を配合したポリエステルよりなる繊−をアルカリ
減量処理して、繊維表両に・、1〜0.IRターンの不
規層な凹凸を付与すると共にこのM^内に1・〜5oo
nすJ#ρンの徽膳な凹凸を存在せしめることによって
色の深みを改善する方法が提案され【いる、 Li−L
ながら、この方′法によって4、色の澱みを改善する効
果は不充分であり、七〇〇上かかる極めて複雑な凹凸形
層によるためか、廖−等め外部からの物理作用により凹
凸が破壊され、破壊された部分が他の破壊されて゛いな
い部分と比べて大きく変色したり、光沢め差を生じたり
、更に4を容易にフイプシル化するという欠点がある。
In addition, a fiber made of polyester containing inorganic particles having a reversibility of less than a diameter of $/Juj turns was subjected to alkali weight reduction treatment, and both surfaces of the fiber were treated with an alkali weight reduction treatment of 1 to 0. In addition to imparting an irregular layer of irregularities to the IR turn, 1.~5oo is added within this M^.
A method has been proposed to improve the depth of color by making the unevenness of the surface appear uneven.
However, this method was not sufficiently effective in improving color stagnation, and the unevenness was destroyed by physical action from the outside, probably due to the extremely complex uneven layer. However, there are disadvantages in that the destroyed part is greatly discolored and has a difference in gloss compared to other unbroken parts, and furthermore, 4 is easily encapsulated.

本発明者は上船欠点のない色の深みと曽明性に優れたポ
リエステル繊維を製造せんとして鋭意検討を行なった結
果、従来の方法ではポリエステルに配合されるポ活性−
機黴粒乎の平麺一次粒子径が100jlJJクロン゛以
上であるか、あるいは平均の一次粒子通が*ooivs
yaン未満の不活性無機超微粒子を使用した場合配合に
よつ七二次凝集が容易に起こって1@@Juミクロン以
上の二次凝集粒子−多欽存在讐るよう゛になるので、結
果的にいず九の場合もポリエステル繊維内部に1・OJ
 JJターン以上の粒子が多数存在し、このためアルカ
曽減量−II&糟によって可I11党−の故長城若しく
はそれ以上の才−〆一の目凸−鐵−表両#I−形成され
、色の深みヤ鱒―性の数置効果を小さくする′と共に耐
フイプ□ル性を劣った一〇にして1%ることを知見し、
この知見に基づいて更に検討−した結果、平均の一次曽
子@が重・・11ξターン未瀦゛であって且つ1・・z
蓼麿ターン以上の二次凝集粒子数が特定の水準以下であ
る不活性黴曽千〇轡定量を含有するポリエステル繊−を
アルカリ処理するととに−よって1wm光−の波長より
も小さな躊′凸を繊維表面の金曹゛k・均一に有するポ
リエステル−繊−が得ら′れ、染色したーの色の欅みと
鮮@性が着L(改善Stすると#に耐フイプ替ル性が楊
段に向上することを鬼出し、先に提案した。
The inventor of the present invention has conducted intensive studies to produce polyester fibers with excellent color depth and brightness that are free from shipping defects, and have found that the polyester fibers that are blended into polyester by conventional methods are
The primary particle diameter of the flat noodle of machine mold grains is 100 JJ JJ cron or more, or the average primary particle size is *ooivs.
When inert inorganic ultrafine particles of less than 1 micron are used, secondary agglomeration easily occurs due to the formulation, resulting in a large number of secondary agglomerated particles of 1 micron or larger. In the case of Target Izuku, 1.OJ is also inside the polyester fiber.
There are many particles larger than JJ turn, and therefore Alka Zeng Weight Loss - II & Kasu is formed by the late great wall of the 11th party - or more talent - 〆1 eye convex - iron - front both #I - and the color. It was found that the numeric effect of depth and trout resistance was reduced by 1% to 10%, which resulted in inferior fip resistance.
As a result of further investigation based on this knowledge, we found that the average primary soma @ is heavy...11ξ turns unreturned and 1...z
When a polyester fiber containing an inert 1,000-meter amount of secondary agglomerated particles with a turn or more is below a certain level is treated with an alkali, a convexity smaller than the wavelength of 1wm light is generated. A polyester fiber having a uniform gold coating on the surface of the fiber is obtained, and the dyed color has a brightness and vividness. I was the first to suggest that he would improve his skills to the next level.

しかしながら、とのようにして得られるポリエステル繊
維は高圧染色でしか染色することかで會ないので、電圧
ボイを染色が可能な墨染量に改質することが望まれる。
However, since the polyester fibers obtained in the above manner can only be dyed by high-pressure dyeing, it is desirable to modify the amount of ink dyeing so that the voltage voids can be dyed.

   −・ 本斃―賓は上記したポリエステル繊維を墨染sK改質す
る方法について種々検討を行なった結果、驚くべきこと
に、上述した不活性微粒子含有ポリニスデルを特定の条
件で高遍紡−することkよってviaな高次黴編構竺を
有する未駕伸繊維となし、しかる後これを非加熱状層で
特定倍率に蔦伸し、次いでてルカー処理を總すこ、とに
よって得た微孔性ポ曽エステル繊維が所期の目的fある
墨染化効果のIIK色の櫟みや幹明性のレベルを更に改
善する効果をもつことを見出した0本発明はこの知見に
基づいて更に検討を重ねた結果完成したものである。
-・The guest of honor has conducted various studies on methods for modifying the above-mentioned polyester fibers with ink-dyed sK, and surprisingly, he has found that the above-mentioned inert fine particle-containing polynisdel can be spun with high spin under specific conditions. Therefore, the microporous porous fiber obtained by forming an unstretched fiber having a high-order molded structure with vias, then stretching it to a specific magnification in a non-heated layer, and then carrying out a lucar treatment. It was discovered that the ester fiber has the effect of further improving the straightness and clarity of the IIK color of the ink dyeing effect, which is the desired purpose.The present invention is the result of further studies based on this knowledge. It is completed.

即ち、本発明は平均の一次粒子径が10@Jリミクロン
未満1ある不活性微粒子を0.1〜S重量う含有し、該
不!竺黴粒子は106111り一ン以上の、下記で定義
する二次am粒子が繊維横断N16平方ミターン当り3
個以上存在しない不活性黴粒子含声ポリエステル繊維で
あって該繊維全体の複層折ムが・、01〜0.14非晶
領域の複屈折んaがOo・・以下、−晶化lll5が3
0%以上のポリエステル未凰伸繊Imを非岬熱状態で1
.05〜*ss@に駕伸し、しか今後アルカ1J611
することに−って駿繊維の少なくとも3重量うを濤#A
(しめることを轡黴キするポリエステル鐵鎗の製造法で
ある。但し、二次a県聴子とは一次粒子径が識別できる
1度に拡大された電子顕微鏡写真で見て、隣接す轡−次
曽子の中心間原画が一次粒子直後の8倍奉、満に接近し
合った状態の着子鮮をいう。
That is, the present invention contains 0.1 to S weight of inert fine particles having an average primary particle diameter of less than 10@J remicrons, The number of secondary AM particles defined below is 1/106111 or more per N16 square mitern across the fiber.
It is an inert mold particle-containing polyester fiber which does not contain more than 10 particles, and the multilayer folding pattern of the entire fiber is 01 to 0.14, and the birefringence a of the amorphous region is Oo. 3
1. 0% or more polyester unstretched Im in a non-heated state
.. It has been extended to 05~*ss@, but in the future Arca 1J611
To do this, use at least 3 weights of fiber #A
(This is a manufacturing method for polyester steel that prevents mold from tightening. However, secondary A-ken is a method of manufacturing polyester iron that prevents the mold from forming. Jisoko's original painting between the centers is 8 times the time immediately after the primary particle, and is a state in which they are completely close to each other.

本li―看の数多(の検討結果の知見によれば、本発明
でい5不活性徽曽千含有ポリエステル繊−が含有する不
活性微粒子は、その平均の一次粒子径が10@jtJf
ク一ン未満でなげればならず、またl(1@IIJ1タ
ーン以−上1.二次凝集着子が繊維横11111・平方
、jクーン当り3個以上存在してはならない、平均の一
次粒子径が1(1・lすlターン以上であったり、10
G191ターン以上の二次凝集粒子が繊維横断菖1・平
方1ターン当り3個以上存在するときは、アルカリ減量
率が低い聰■で充分な色の深みと鮮明性が得られず、遂
に充分な色の深みと鮮明性を得ようとしたり嵐い風合を
出そ、う3としてアルカリ減量率を大きくすると耐摩擦
耐久性や耐フイブリル性が悪くなり実用上問題を生じる
According to the knowledge of the study results of numerous studies, the inert fine particles contained in the inert polyester fiber of the present invention have an average primary particle diameter of 10@jtJf.
The average primary If the particle size is 1 (1.1 turns or more) or 10
G19 When there are 3 or more secondary agglomerated particles of 1 turn or more per 1 square turn of the cross-fiber irises, sufficient color depth and clarity cannot be obtained with the low alkali loss rate, and finally, sufficient color depth and clarity cannot be obtained. In order to obtain depth and vividness of color or to create a stormy texture, increasing the alkali weight loss ratio deteriorates the abrasion resistance and fibrillation resistance, causing practical problems.

平均の一次粒子径としては、なかで4soiリミターン
以下の範囲が好ましく、30ミリミクロン以下の範囲が
41に好ましい。また、繊維横断面”1 ’O”平方1
クー′ン′当りに存在する二次凝集粒子数とし゛ては、
なかでも2個未満であるのが□好ましく%111未満で
あるのが4IK好′ましい。
The average primary particle diameter is preferably in the range of 4 soi limiters or less, and more preferably in the range of 30 mm or less. In addition, the fiber cross section "1'O" square 1
The number of secondary agglomerated particles present per Ku'un' is:
Among these, it is preferable that the number is less than 2, and 4IK is preferably less than 111%.

′本発明でいう一次粒子直後とは該−次粒子と゛同じ容
積を有する想像上の球のJ[径を意味する。
'Immediately after the primary particle in the present invention means the diameter J of an imaginary sphere having the same volume as the primary particle.

また、二次凝集粒子とは一久粒手がその一次粒子径より
小さい関′隔、即ち隣接する一次着子″め中心間”の距
虐が該−次粒子径の2倍未満に@近′し合った状態の粒
子#を意味し、この二次凝集粒子の端から端までの距離
が最大のところを二次凝集粒子の”大きさ滅するすこの
定−゛による二次凝集粒子は一次粒子径が織q:j!き
る横置に拡大された電子顕微鏡写真によってIIN姦す
ることができる。
In addition, secondary agglomerated particles are particles with a separation smaller than their primary particle diameter, that is, the distance between adjacent primary particles "to the center" is less than twice the diameter of the primary particle. This refers to particles in a state where they are mixed together, and the distance from one end to the other of these secondary agglomerated particles is the maximum, and the secondary agglomerated particles are considered to be primary particles according to the constant of decreasing size of the secondary agglomerated particles. IIN can be seen by an electron micrograph magnified in horizontal orientation with a diameter of 100 mm.

本発明でいう不活性徴粒子は、ポリエステル繊鎗中に前
記した如く分散し得るポリニスフルに不゛活性の微粒子
であれば*に@定する必要はな(、例えばシリカゲル・
、アルlすを含有するか叉は含有しないシ曽力、アルi
すlkl働粒子状アルlす、極黴曽駿化チタイ、炭酸カ
ルシウムゾル、徹曽子状炭酸カルシウ^等の無4−曽子
やリンイど合”物と金属化合物とをポリエ1ル反応系内
部で反応−させて析出せしめたPII@柄出系黴曽子等
が好ましく、なかでも後で詳し\鋭嘴する(1)下記一
般式  ・ 鳳 r 化合物及び/叉はリチウ^化合物とからなる内郁析出系
徽載子が41に好ましい、上記の不活性微粒子はポリエ
ステル繊維E1種のみ単独で含有されても、また3種以
上が一部に含有stしてかかる不活性微粒子の含有量は
、あまりに少ないときには最終的に得られるポリエステ
ル繊&!の表11i!16−不充分となり色の諏みや鱒
−性(L善効果が−められ―(、この量を多(する従っ
て・・j、の欅みや鮮明性は増加するが、あま−に  
なると最早色の深みや鮮明性は著しくek  Aさず、
かえって耐フィプ曽ル性が悪化ダ ようになり、その上
紡糸が極めてmsとな事実上不可部な実施範囲となる。
The inert particles in the present invention do not need to be defined as *@, as long as they are fine particles that are inactive to polynisfuls and can be dispersed in polyester fibers as described above (e.g., silica gel, etc.).
, containing or not containing aluminum, aluminum
A polyester reaction system in which a metal compound is combined with a 4-free compound or a phosphorus compound such as a particulate aluminum, a calcium carbonate sol, or a calcium carbonate sol, and a metallic compound. Preferably, PII is precipitated by internal reaction, and is particularly preferred, as will be explained in detail later. Preferably, the inert fine particles of 41 are precipitated, and even if the above-mentioned inert fine particles contain only one type of polyester fiber E, or if three or more types are partially contained, the content of such inert fine particles is If the amount is too small, the amount of polyester fibers finally obtained will be insufficient, resulting in color blurring and graininess (L-improving effect). , the intensity and sharpness of the image increases, but it is not very
When this happens, the depth and clarity of the colors will no longer be noticeable.
On the contrary, the filip resistance deteriorates, and moreover, the spinning speed becomes extremely high, which is practically an indispensable practice range.

このため、不活性微粒子の含有量は・、1〜S重量囁の
範■とする必要があり、なかで40.1〜1腫量囁の範
1が好ましい。
For this reason, the content of the inert fine particles needs to be in the range of 1 to 100% by weight, and preferably 40.1 to 100% by weight.

零発−でいうポリエステルは、テレフタル−を主たる酸
成分とし、少なくとも1種のグリコール、好ましくはエ
チレングリー−ル、トリメチレン/vコール、テトラメ
チレンダリコールから選ば九た少なくともillのフル
キレンダ曽コールを主たるダ曽ツール威分とするポリエ
ステルを主たる対象とする。
The polyester in the term "zero starting" has terephthalic acid as its main acid component, and at least one kind of glycol, preferably ethylene glycol, trimethylene/vcol, tetramethylene dalycol, and at least nine full kylene dalycols as the main acid component. The main target is polyester, which is the specialty of Daso tools.

また、テレフタル鹸虞分の一部を倫の二富簡Ikカルボ
ン鐙威分で置換えたポリエステルであってもよく、及び
/叉はダ曽・−ル威分あ一部を主威秀以外の上記グリコ
ール、若しくは倫のジオール成分で置換えたポリエステ
ルであってもよい。
It may also be a polyester in which part of the terephthalic acid content is replaced with Lun's Erfukan Ik Carvone oxidative content, and/or a part of the terephthalic acid content is replaced with a material other than Lord Weixiu. It may also be a polyester substituted with the above-mentioned glycol or a diol component.

ここで使用されるテレフタル酸以外の二官能性カルボン
酸としては、例えばイソフタル酸。
The difunctional carboxylic acid other than terephthalic acid used here is, for example, isophthalic acid.

ナツタ曽ンジカルポン酸、a)フェニルジカルモノ駿、
ジアエノキシエタンジカルポン酸、I−ヒトーキシエト
中シ安息書酸、P−オ中シ安息香s1.暴−ナト曽つム
スル永インフタル酸、了りビン駿、セバシン臆、1.4
−ジターへキすンジカルボン駿の如會芳香族、脂肪族、
脂場族の二官能性カルボンlI!をあげることができる
。また、上記ダ曽コー□ル以外のジオール化合物として
は例えばジターへ中ナンー!、4−ジメタツール、ネオ
ペンチルダl:s−ル、ビスフェノールム、ビスフェノ
ール8の如き脂肪族−脂環族−芳香族のジオール化合物
およびポ替オキジアルキレンダリコール等をあげること
ができる。
Natsutason dicarboxylic acid, a) phenyl dicarboxylic acid,
Diaenoxyethane dicarboxylic acid, cybenzoic acid in I-hydroxyethane, cybenzoic acid in P-oxyethane s1. 1.4
- Aromatic, aliphatic, dicarboxylic acid,
Bifunctional carvone lI of the fatba family! can be given. In addition, examples of diol compounds other than the above-mentioned Dasokoru include Jitter to Nakanan! , 4-dimetatool, neopentyldalyl, bisphenol, bisphenol, aliphatic-alicyclic-aromatic diol compounds such as bisphenol 8, and polyoxydialkylene dalicols.

かかるポリエステルは任意の方法によって製造したもの
!よい、儒九ばポリエチレンテレフタレートについて説
−す九ば1通常、テレフタル酸とエチレングリコールと
を直接エステル化反応させるか、テレフタル酸ジメチル
の如きテレフタル酸の低級アルキルエステルとエチレン
グリコールとをエステル交換反応させるか又11テレフ
タル酸とエチレンオキ量イドとを反応させるかしてテレ
フタル酸のダ12−ルエステル及び/叉はその低重合体
を生成させる第1段階の反応と、嬉1段階の反応生成物
を減圧下加熱して所望の重合JIKなるまで重縮合反応
S(る第sH階の反応によって製造Stする。
Such polyester can be produced by any method! Good, Confucian explanation about polyethylene terephthalate - 1 Usually, terephthalic acid and ethylene glycol are directly esterified, or lower alkyl esters of terephthalic acid such as dimethyl terephthalate are transesterified with ethylene glycol. Alternatively, the first stage reaction is to react 11-terephthalic acid with ethylene oxyhydride to produce a d-12-terephthalic acid ester and/or its low polymer, and the reaction product of the first stage is depressurized. Under heating, the product is produced by a polycondensation reaction S (sH stage reaction) until the desired polymerization JIK is obtained.

本11嘴でいう不活性微粒子含有ポリエステルは任意の
方法によって調達することができるが、41に前述した
ポリエステルの展進が完了するまでの任意の段階で(s
l)鍍ポ替エステルな構成する酸成分に@して・、1〜
島モルラの下記一般式%式% で表わさ九る曽ン化舎物及び伽)アルカリ土類金異化舎
物及び/叉は曽チク^化舎物を(−と(−とを予め反応
させることな(1つ(−と−の金属の犠量歇の舎曽量−
一の曽ン化会物のそル道に対しC亀・〜1.3普となる
ように添加し、しかる後ポリエステルの脅威を完了する
方法が好ましく採用される。
The inert fine particle-containing polyester referred to in Book 11 can be procured by any method, but at any stage until the polyester expansion is completed as described in 41 (s
l) For the acid component constituting the ester, 1~
By reacting (- and (-) in advance, the alkaline earth metal catabolism and/or the chloride represented by the following general formula % formula % of Shima Morura) (1 (- and - metal sacrificial quantity -
A preferred method is to add C to 1.3% to the total amount of polyester, and then to complete the removal of polyester.

ここで使用する曽ン化會物は下記一般式%式% で表わされるリン化合物であり、式中翼1及び鼠1は水
素原子又は−優の有機基である。この−価の有機基は異
体的にはアル中ル基、アリール基。
The compound used here is a phosphorus compound represented by the general formula % below, where 1 and 1 are hydrogen atoms or organic groups. This -valent organic group is an alkyl group or an aryl group.

794キル基又it t(C&)4G)kl” (但し
、rst水嵩原子、アル中ル基、ア曽−ル基叉は7ラル
キル基、Iは2以上の整数、には1以上の整数3)等が
好ましく、R′とVとは同一でも異なっていてもよい、
Xは水素原子、−価の有機基又は金属!あり、−価の有
機基としては上記1k”、Il”Kおける有機基の定義
と同様であってS R@I R”と同一でも異なってい
てもよく、また金属としては特にアルカリ金属−アルカ
リ土類金gが好ましく、なかでもアルカリ土類金属が4
1に好ましい、mはO又は1の整数である。
794 kyl group or it t(C&)4G)kl'' (However, rst water bulk atom, alkyl group, azol group or 7ralkyl group, I is an integer of 2 or more, and 3 is an integer of 1 or more) etc., and R' and V may be the same or different,
X is a hydrogen atom, a -valent organic group, or a metal! The -valent organic group is the same as the definition of the organic group in 1k'' and Il''K above, and may be the same as or different from SR@IR'', and the metal is particularly alkali metal-alkali. Earth gold is preferred, especially alkaline earth metals
1, m is an integer of O or 1.

かかるリン化合物としては、例えば正リン酸。Examples of such phosphorus compounds include orthophosphoric acid.

リン酸トリメチル、リン酸トリメチル、9ン一トリプチ
ルsly歳)17エ二ルのよ5な□ン酸トリエステル、
メチルア1ド゛ホスフエート。
trimethyl phosphate, trimethyl phosphate;
Methyl 1 dephosphate.

エチルア膚ドホス7エートープチル月ドホス7エートの
ようなリン114ノ及びジエステル。
Phosphorus-114 and diesters such as ethyl-dophos-7-ethopyl-dophos-7ate.

Mリン酸−鳳蓼装置トリメチル、lieン酸トリエチル
−厘曽ン鐙トリプチルクjl−ン駿トリフェニルのよう
なIllン@)Vエステルーメチルアシドホスアアイト
ーエチルアシドホスファイシ、ブチルアシドホスファイ
トのような亜すン酸七ノ及びジエステル、上[1ン化舎
物をダリコール及び/叉は水と反応させるととにより得
られるシン化合物、更に上記したリン化合物と所定量の
対応する金属の化合物とを11謙の存在下−m反応さ4
kToことによって得もtLるリン化合物等から選ばれ
た1種以上のシン化合物な用いることがで會る。なお、
上記したシン化合物と金属化合物とを反応させる際の濤
厳としては、対象ポリエステルの原料として使用するグ
曽ツールを使用するのが最も好ましい。
M phosphate - trimethyl, triethyl phosphate - triphenyl triphenyl, V ester - methyl acid phosphatide, butyl acid phosphite and diesters of phosphorous acid, phosphorus compounds obtained by reacting phosphorous compounds with dalicol and/or water, and phosphorous compounds as described above and a predetermined amount of the corresponding metal. The compound is reacted with 11-m in the presence of 4
It is also possible to use one or more sulfur compounds selected from phosphorus compounds and the like. In addition,
When reacting the above-described syn compound and metal compound, it is most preferable to use the Guso tool used as a raw material for the target polyester.

上記リン化−合物に併用するアルカリ土類金属化合物及
びリチウム化合物よりなる鮮から選ばれる金属化合物と
しては上記のリン化合物と反応してポリエステルに不鋳
懺の金属塩な形成するものであれば4Iに制限はない0
例えばMg。
The metal compound selected from the group consisting of alkaline earth metal compounds and lithium compounds to be used in combination with the above phosphorus compound is one that reacts with the above phosphorus compound to form an uncastable metal salt in the polyester. There is no limit to 4I0
For example, Mg.

Cas are Baa Llの一一塩、しゆう酸塩、
安息香酸塩、フタル酸塩、ステアリン酸塩のような有機
力^ボン酸塩、硼酸塩、硫酸塩、*a塩、炭11重炭酸
塩の如き無機酸塩、塩化物のようなハーゲン化物、エチ
レンシア1ン4−鐵舞塩のようなキレート化合物、水酸
化物書酸化−〇メチラート、エチラート−グリコレート
等のフルコラート類、フェノラート等をあげることがで
きる@41にエチレンダリコールKWIl性である有機
カルボン酸塩、八−ゲン化物、キレート化舎物、アルツ
ラニシが好ましく、なかでも有機カルボン酸塩が41に
好家りい、上記のアルカリ土類金属化合物及び蓼チ9′
^化合物は1種のみ単独で使用しても、また8種以上併
用してもよい。
Cas are Baa Ll monosalt, oxalate,
Organic salts such as benzoates, phthalates, stearates, borates, sulfates, *a salts, inorganic salts such as carbon-11 bicarbonates, hagenides such as chlorides, Examples include chelate compounds such as ethylene cyanide 4-metallic salt, fluorates such as oxidized methylate, ethylate-glycolate, phenolate, etc.@41 is ethylene dalycol KWIl. Preferred are organic carboxylates, octogenides, chelated compounds, and Alturanisi, and among them, organic carboxylates are preferred for 41, the above-mentioned alkaline earth metal compounds, and alkaline earth metal compounds.
^ Compounds may be used alone or in combination of eight or more.

上記リン化合物及び金属化合物を添加するに当って、最
終的に得られるボVエステル繊Iak優れた色の深みと
その摩擦耐久11を与えるためKは、シン化合物の使用
量及び*Wン化會物の使用量に対する金属化合物の使用
量の比を善定する必要がある。jlち、本発−で使用す
るシン化合物の添加量−1あま9に少ないと最終的に得
bfLるポ讐エステル繊鎗の色の―みが不充分にな9、
この量を多くするEl!つて色の概みは増加するが、あ
まりに多くなると最早もの欅みは着しい向上な示魯ず、
かえって摩擦耐久性が悪化し、その上充分な重合度と軟
化点を有するポリエステルを得ることが開離となり、更
に艙来時に糸@tL−多、−′するというトラブルを発
生する・このためリン化合物の添加量はポリエステルを
構成する酸成分に対してO,S〜m4ル弊の範−にすべ
會でkす、411に・、S〜8モルラの範■が好ましい
、また、上記リン化合物と金属化合物に含まれる金属の
当量数の合計量がリン化合物の七ル歇に対して先・倍よ
り少ない量では、得られるポ讐エステル繊鎗の色の欅み
が不充分であり、その上重縮合適度が低下し^重合度の
ポリエステルな得ることが開離となり、また生成ポVニ
スデルの歇化点−大幅に低下するよ5になる。逆にこの
量が1.諺倍な趨九1と糎大誼子が生成し、色の深みは
改善されるどころか、かえって視感濃度が低下するよう
になる。このため上記リン化合物と金−化合物の金属の
当量数の合計量は酸リン化合物のモル数に対してj O
〜3−3倍の範■になる量にすべきであり、411に!
、O−3.0倍の範囲が好ましい。
When adding the above-mentioned phosphorus compound and metal compound, in order to give the finally obtained Bo V ester fiber Iak excellent color depth and its friction durability 11, K is determined by the amount of the phosphorus compound used and * It is necessary to determine the ratio of the amount of metal compound used to the amount of metal compound used. However, if the amount of the compound used in the present invention is less than 1/9, the final color of the polyester yarn obtained will be insufficient.
El to increase this amount! As the color increases, the overall appearance of the color will increase, but if it becomes too large, the color will no longer show any signs of improvement.
On the contrary, the friction durability deteriorates, and in addition, it becomes difficult to obtain a polyester with a sufficient degree of polymerization and softening point, which causes problems such as threads forming when carrying. The amount of the compound to be added should be within the range of O, S to m4 to the acid component constituting the polyester, preferably in the range of 411 to S to 8 molar. If the total number of equivalents of metals contained in the metal compound is less than 7 times the amount of the phosphorus compound, the color of the obtained polyester fiber will be insufficient; The degree of polycondensation decreases, the degree of polymerization of the polyester becomes dissociated, and the tempering point of the polyester produced decreases significantly to 5. Conversely, this amount is 1. The proverbial trend 91 and tacky color are generated, and instead of improving the depth of color, the visual density actually decreases. Therefore, the total number of metal equivalents of the above-mentioned phosphorus compound and gold compound is j O
The amount should be ~3-3 times the range ■, which is 411!
, O-3.0 times is preferred.

l記すン化合物と金属化合物とは予め反応させることな
くポリエステル反応層に添加する必要がある。とうする
ととkよって、不溶性粒子をポリエステル中に均一な超
微粒子状態で生成せしめることかできるようkなる。予
め外部ヤ上記リン化合物と金属化合物とを反応させて不
溶性粒子とした後tAvニスチル反応系に添加したので
は、ポリエステル中での不溶性粒子の分散性が−(なり
且つ粗大凝集粒子が含有きれるようkなるため、最終的
に得られるポリエステル繊維の也の深みを改善する効果
は鑓められなくなるので好ましくない、     ゛上
記のリン化合物及び金属化合物の添加は、それぞれポリ
エステルの一造が完了するまでの任意の段階において任
意の層厚で行な5ことができる。しかし、9741合物
の添加時期が一五段階の反応が未終了の段階では481
49階の反応の完結が阻書されることがあり、またかか
る多量の金属化合物を菖1段階の反応終了前Kl加する
と、この反応がエステル化反応のときは、この反応中に
粗大粒子が発生したり、エステル交換反応す表きはこの
反応が異常に早(進行し央沸′現象を引起こすことがあ
るので、この場合その一20重量シ一度以下にするのが
好ましい。
It is necessary to add the compound mentioned above and the metal compound to the polyester reaction layer without reacting them in advance. As a result, it becomes possible to form insoluble particles in the polyester in the form of uniform ultrafine particles. If the external phosphorus compound and metal compound are reacted in advance to form insoluble particles and then added to the tAv Nistil reaction system, the dispersibility of the insoluble particles in the polyester becomes - (and the coarse agglomerated particles are completely contained). This is undesirable because the effect of improving the depth of the polyester fiber finally obtained cannot be diminished. ゛The addition of the above-mentioned phosphorus compound and metal compound is necessary until the polyester fabrication is completed. It can be carried out at any stage and with any layer thickness.However, if the timing of addition of 9741 compound is not completed before the reaction of stage 15 is completed, 481
Completion of the reaction on the 49th floor may be inhibited, and if such a large amount of metal compound is added before the completion of the 1st stage reaction, if this reaction is an esterification reaction, coarse particles may be generated during this reaction. If transesterification occurs or transesterification occurs, this reaction may proceed abnormally quickly and cause a mid-boiling phenomenon.

金属化合物の少な(とも80重量う及びリン化合物の全
量の添加時期はポリ−ステルの合成の第1段階の反応が
実質的に終了した段階以降であることが好まし1%、ま
た、リン化合物及び金属化合物の添加時期が、継型段階
の反応があまりに進行した段階では1粒子の凝集、11
大化が生じ易(最終的に得られるポリエステル繊維め色
の欅みが不充分となる傾向があるので、II2段階の反
応#Cおける厘応晶合物の極限粘度がe、s ec g
適する以前!あることが好ましい。
It is preferable that the amount of the metal compound (both 80% by weight) and the total amount of the phosphorus compound be added after the stage where the reaction in the first stage of polyester synthesis is substantially completed. If the time of addition of the metal compound and the reaction at the joint stage has progressed too much, agglomeration of one particle or 11 particles may occur.
(Because the final polyester fiber color tends to be insufficient, the limiting viscosity of the polyester compound in reaction #C of II 2nd step is e, s ec g.
Before it was suitable! It is preferable that there be.

上記のリン化合物′及び金−化合物は、それぞれ一時に
添加しても、8g1以上に分割して添加し′ても、又は
連続的11c−一′してもよい。
The above-mentioned phosphorus compound' and gold compound may be added all at once, in portions of 8 g or more, or may be added continuously.

ポリエステル製造・の第1段階の反応に任意の触媒を使
用する゛ことができるが、上記金属化合物の中□でtI
m1段階の反応、41にエステル交換反一応の触厳能を
有するものがあり、゛かかる化合物を使用する場合はm
K触媒を使用することを要さず、この金属化i物な嬉s
R階のff応闘紬前゛又は反応中に添加して、触媒とし
ても兼用することができるが、前述し麩如<嬌沸現象瘉
引起こすことがあるめで、その使用量は添−する金属化
合物6全量の!O重量繁未満にとどめるのが好ましい、
パ 本発明に■いては、譲りエステル未延伸繊―として、゛
曽通の如き不活性徴粒子含有ポーエステルからなり、亘
つ、繊−全体・と゛してはかなり高度の配向性と結晶性
とを有する#Ic4かかわらす非晶領域はきわめて低度
の配向性しか有しないという特殊な一細構造を一つ繊維
を使用する。
Any catalyst can be used in the first step reaction of polyester production, but in the above metal compound, tI
There are compounds that have some ability to catalyze the transesterification reaction in the m1 stage reaction, and if such compounds are used,
This metallized product does not require the use of a K catalyst.
It can also be added as a catalyst by adding it before or during the reaction, but as mentioned above it may cause the boiling phenomenon, so the amount to be used is not included. Total amount of 6 metal compounds! It is preferable to keep the weight to less than 0.
In the present invention, the undrawn ester fiber is made of polyester containing inert particles such as Sotsu, and the fiber as a whole has a fairly high degree of orientation and crystallinity. A fiber with a special fine structure in which the amorphous region has only a very low degree of orientation is used.

即ち、皺繊維は、繊―全体の複層llIrへ、非晶領域
の複層折ムa及び麹晶化度X−が下記条件のす。
That is, in the wrinkled fiber, the multi-layer folding pattern a of the amorphous region and the koji crystallinity X- of the entire fiber meet the following conditions.

ぺてを横尾するものである。  −26ム・−−・、・
t〜@、1−4C好ましくは0.01〜0.11)Xs
  =−*・%以上  (好ましくは4・繁以上)八l
−−・、・6以下  (好ましくはO,・1〜G、(1
4)ごのよ5な未駕伸繊鎗は、後述の非加熱状態での駕
伸が容品であり、しかも、かかる蔦伸によって自着性、
陶Jll愉及び熱的・機械的性質のすぐれた鐵−とする
ことができる。
It is a side effect of Pete. -26mu・---・・・
t~@, 1-4C preferably 0.01~0.11)Xs
=-*・% or more (preferably 4・Ten or more) 8l
--・,・6 or less (preferably O,・1~G, (1
4) The stiff, non-carved stretching spear can be rolled in a non-heated state as described below, and furthermore, it has good self-adhesive properties due to such stretching.
It can be used as a ceramic material and as an iron with excellent thermal and mechanical properties.

しかるに、繊織全体の複JiIFrムが、・、O!より
低い場會、lI伸時の分子鎖の変形量が大きく、台分子
鎖に働(応力の分布(4大きな広がりができるため、非
細鵬檎腸での延伸性が劣り、予熱ローラ等を眉いて駕伸
温Jlll!をあげても凰伸斑が起りやすい、一方、ム
が0,14を履えるものは、過電、1・・・17分より
高速’t’#Aする必要が島るため一畳別轟Ik−の巻
取装置を要し設備コストが大になるばかりでなく1品質
−にも空気抵拡によるデニールの均−妹の低下が著しく
、特Kjl11デニール糸の場合には糸切れを伴い安定
な操業は望み得ない また、ムが0.14より大きいと
非加熱状態での延伸において延伸張力が高(なり延伸繊
維の機械的特性が低下する。
However, the composite JiIFrm of the entire textile is...O! At lower temperatures, the amount of deformation of the molecular chains during II stretching is large, and the stress distribution (distribution of stress) acting on the molecular chains is large, resulting in poor stretchability in non-thin ingots, and the need for preheating rollers, etc. Even if you raise your eyebrows and raise your eyebrows, elongation spots are likely to occur.On the other hand, those who can wear MU of 0,14 need to run at high speed 't'#A for 1...17 minutes. Not only does this require a separate winding device for each tatami mat, which increases the equipment cost, but also the uniformity of denier decreases significantly due to air resistance, especially in the case of Kjl11 denier yarn. In addition, if the m is larger than 0.14, the stretching tension will be high during stretching in an unheated state (as a result, the mechanical properties of the drawn fibers will deteriorate).

一方、未延伸繊維の結晶化度XeがSO%に満たない場
合、これから得られる延伸繊維は高配−非結晶ともいう
べき微細構造となり、熱く対する安定性を全く欠いてい
るため、改めて180’−tso℃11度の熱セッシを
要し、駿備コスト。
On the other hand, if the crystallinity Xe of the undrawn fibers is less than SO%, the drawn fibers obtained therefrom will have a fine structure that can be called highly oriented-amorphous and lack stability against heat. It requires heat treatment at a temperature of 11 degrees Celsius, which is expensive.

エネルギーコストの増加をもたらす他、熱セット斑を避
けることが難しく繊維の均染性を悪化させてしまう。
In addition to increasing energy costs, it is difficult to avoid heat-setting unevenness, which worsens the level dyeing properties of fibers.

本尭明では、上記未延伸繊維におい℃、繊維全体の複屈
折An及び結晶!L度Xc K加些、非晶領域、41に
結晶と結午な結びつけている分子(ti・moL@eu
l・)の配向性!1重−であっ【、非晶領域の複屈折Δ
naがO,am以下であることが必要である。−ち、結
晶量に分布する非晶分子鎖の配向凝集性が鳥いと、延伸
は多くの分子鎖の拭がり(unfoiding) k伴
い上記結晶の破壊をもたらすことになり延伸斑が爛りヤ
すくなるばかりでなく、4にめて鶏セットの必I!性が
生じて(る。
At Takaaki Moto, the undrawn fibers have temperature, birefringence An and crystals of the entire fiber! L degree
l・) orientation! Single-fold [, birefringence Δ of the amorphous region
It is necessary that na be equal to or less than O, am. - First, if the orientational cohesion of the amorphous molecular chains distributed in the amount of crystals is high, stretching will cause many molecular chains to be undone (unfoided), resulting in the destruction of the crystals and the stretching unevenness. Not only is it a must-have, but it's also a must-have for any chicken set! Sexuality has arisen.

つまり、あるS度以上に配向し、発達した結晶が拘束性
の低い非晶によって結びつげられている場合にのみ、非
m鴎下での低倍率の延伸により結晶の破壊を伴わない再
配置が可能であ11、酷セットの必要もなく染着性、均
染性にすぐれ、通常の蔦伸熱逃職糸と同様の熱的・機械
的性質を持つポリエステル繊維を得ることが可能である
In other words, only when crystals that are oriented at a certain degree of S or more and are connected by amorphous materials with low restraint can rearrange the crystals without destroying them by stretching at a low magnification under a non-magnifying glass. It is possible to obtain polyester fibers that have excellent dyeability and leveling properties without the need for severe setting, and have the same thermal and mechanical properties as ordinary ivy-drawn heat escape yarns.

なお、ここ1言ラム、八1及びXeは、それぞれ次の方
法によI) @ fi 8れる値である。
In addition, here, 1 word Ram, 81, and Xe are values obtained by the following method, respectively.

鳳)ム(値組1:繊―軸に対して直角に偏光しているf
f1K対する複M祈率(n土)と繊維軸に対して平行に
偏光している光に対する属祈皐(論証)との値、*ち4
1\1寓a厘−n↓で表される。ペレッタコンベンセー
ターを義着した偏光馴徴鏡を層い、電鉄により欄定され
る。(ただし、浸液としくト警タレジル7オスフエート
を使用、) 層) Δna (非晶領域の複屈折)二非晶領域の分子
鎖の配向性を示すパラメータであり比重pより求める1
11$1複J1祈率ム、結蟲配崗画歇fe(41MM 
@ 0− s si *m 号’A報記載) klfi
イて次式により算出する。
Feng) Mu (value set 1: fiber - f which is polarized at right angles to the axis
The value of the compound M ratio (n) for f1K and the ratio (demonstration) for light polarized parallel to the fiber axis, *chi4
It is expressed as 1 \ 1 f a rin - n ↓. A polarizing mirror equipped with a Peretta convensator was installed and the field was fixed by the electric railway. (However, the immersion liquid used was Taresyl 7 osphate.) Δna (birefringence of amorphous region) 2 A parameter that indicates the orientation of molecular chains in the amorphous region, determined from the specific gravity p1
11$1 double J1 prayer rate, yuibugaigangga fe (41MM
@ 0-s si *m issue 'A report) klfi
Calculate using the following formula.

ff1LXz= (41,7491−’)/QJ@17
8■)Xe(結晶化−)   ゛ X線回折で赤道方向w−現れ一′ポリーステルフィラメ
ントの(OSO)画の鑓祈“’IIRt−館1111の
如く空気数置の補正後l@とIaK分■し、次式により
求める。
ff1LXz= (41,7491-')/QJ@17
8■) It is calculated by the following formula.

’(re/(Ia+4m ) ) X 1 tjDmX
e(%) “(Xalll折は理学電機mD−1cal
all置を用い、欄定条件はsslマ×意@m、組−フ
イ′ルター使用、ダイバージェンスス スキャッタ′リンダスリットt、レシービンダスリット
@、B Mとする。) このような黴1構造を有する不話性徴曽子含有ポリエス
テル未駕伸繊維t−製造する虻は、上記゛不m性徹粒子
會”有゛ポリエステルを1III来口金より溶融吐出し
、吐幽蟲条を冷却固化後4000〜7・・・m/分口好
ましくは41・〜$600./分で引取る方法が、生−
′性及び得られる未延伸繊維の均一性がすぐれているた
め好ましい、しかし−1これ以外にも、紡糸口金の孔i
を太き(して、繍4rラフ)knees以上にあげ上′
記引取適度を31′0・諺/分以上とする方法や、紡糸
口金から吐出されたA東がいったん該ポリエステルのガ
ラス転移−R以下まで冷却したのち、加熱曽、ス1ット
ヒーfi−、z熱−一う−等により場−に1糞0〜夏6
・’CKNJEIIIn、しかる11si・・II/1
以上で引取る方法などを採用す−こともできる。
'(re/(Ia+4m)) X 1 tjDmX
e(%) “(Xall fold is Rigaku mD-1cal
The all setting is used, and the field conditions are ssl ma x y@m, set-filter use, divergence scatter linda slit t, receiver slit @, BM. ) The fly to produce the undrawn fibers of polyester containing non-talking particles having the mold structure is melted and discharged from a die using the above-mentioned polyester having an "immature particle permeability". After cooling and solidifying the rods, the raw material is collected at a rate of 4,000 to 7...m/min, preferably 41 to $600./min.
It is preferable because of its excellent properties and the uniformity of the resulting undrawn fibers.
Thick (and embroidery 4R rough) above the knees
There is a method in which the withdrawal rate is set to 31'0/min or more, and after the A east discharged from the spinneret is once cooled to below the glass transition -R of the polyester, it is heated, heated, heated, etc. 1 feces 0 to 6 in summer due to heat etc.
・'CKNJEIIIn, scold 11si...II/1
It is also possible to adopt the above-mentioned collection method.

ここ!#出するIlmはφ!!部を有しない中夷繊鐘で
≦っても、中!IIIを有する中空繊維であってもよい
、゛重゛たl11mの横断Hk1する外形や中空部の形
状は内海であっても異形であってもよい、更に前記の不
m性黴毅子を含有する変性ポリエステルと含有しない未
変性ポリエステルからなり、変性ポリエステルな鞘成分
とし、未変性ポリエステルを芯成分とする芯鞘IIII
合繊維であっても、変性ポリエステルと未変性ポリエス
テルとからなる8層又はそれ以上の多層のすイド・ノ(
イ・サイド1複合繊−でもよい。
here! #Ilm to issue is φ! ! Even if it is ≦ in the Zhongyi Sensho that does not have a part, it is in the middle! It may be a hollow fiber having a 11 m cross section Hk1, and the shape of the hollow part may be inland or irregular. A core-sheath III consisting of a modified polyester that contains a polyester and an unmodified polyester that does not contain a modified polyester, a sheath component that is a modified polyester, and a core component that is an unmodified polyester.
Even if it is a synthetic fiber, it has eight or more layers of modified polyester and unmodified polyester.
Side 1 Composite fibers may also be used.

零発1jKよれば、かかる未蔦伸鐵艙は、郭加熱状簡で
i、as 〜1.1!1倍、好ましくは1.1・〜t1
me倍に鷺伸する。この鷺伸は溶融紡糸後いったんパッ
ケージにIalllつた後、舅ニーで行ってもよいが、
紡糸した繊維を41)職ることな(連続して行う、いわ
ゆる鋳蟲直111蔦伸を行って設備スペースの減少、省
力化等をはかることもできる。
According to the zero-hatsu 1jK, such a non-tsuta extension train is i, as ~1.1!1 times, preferably 1.1.~t1 in the heating form.
Stretch it twice as much. This heron stretching can be done with the knee after melt spinning and once it is put into the package, but
It is also possible to reduce the equipment space, save labor, etc. by subjecting the spun fibers to continuous (continuous) so-called casting straight 111 stretching.

通常、ポ警エステル未蔦伸繊維は、ポリエステルのガラ
ス転審議度より高温で駕伸され更に約130−100℃
の温度で熱セットさ九るが本発明で使用する不活性黴曽
子含有ポリエステル未駕伸繊纏は、前述の如き畳殊な黴
−構造なあり、Lか4冷駕伸によつ″C粂着性、均粂性
にすぐれ寸法安j1銖の良好な繊維が得られる。
Normally, polyester untsuta-stretched fibers are stretched at a temperature higher than the glass transition temperature of polyester, and then further stretched to approximately 130-100°C.
The inert mold-containing polyester unstretched woven fabric used in the present invention can be heat-set at a temperature of C. Fibers with excellent gluing properties and uniformity, and good dimensional stability can be obtained.

(11つてll来の細會鴎七ットは不要である・)とこ
ろがm蔦伸を行うと、紬糸段階で形成された易染性の機
織構造が破塵stL″clII着性が低下するばかりで
なく、m繊維を全(均−KJO熱することが−しく、ま
た鍍繊鍾は僅かの温度斑によつC4m斑が発生するため
、均粂性の晶化がさけられない、なお、蔦伸熱によって
−−ラの温度がガラス転審温直以上に上昇する場合は、
−−ツ内@に冷却水な過水して−−ラ表Wを室温付gK
鋤持するのが良い、蔦伸普率は1.・暴#1−g、am
普(好まL<4!1,1@ 〜1.1@倍)とする必要
がある。lI伸僑率が1.0@未満では鷺伸の効Jlが
芝L<1機械的性質(智爾強皮、切断伸度、一次降伏点
値魔等)が全般的に劣ったものとなり、蔦−倍率が13
111七趨えると蔦伸11が晶化するのみならず、18
ら詐る繊膳の強fIK−非雷IC低くなる。
(11) However, when m-tsuta stretching is performed, the easily dyeable woven structure formed at the pongee thread stage only deteriorates the adhesion of dust stL''clII. However, it is preferable to uniformly heat the M fibers evenly, and C4m unevenness occurs due to slight temperature unevenness in the plating process, so uniform crystallization cannot be avoided. If the temperature of the glass rises above the temperature of the glass due to heat expansion,
--- Fill the inside with cooling water --- La table W at room temperature gK
It is better to carry a plow, the growth rate of vines is 1.・Bang #1-g, am
(preferably L<4!1,1@~1.1@x). When the lI elongation rate is less than 1.0@, the effectiveness of the heron elongation Jl is L<1, and the mechanical properties (chier toughness, cutting elongation, primary yield point value, etc.) are generally inferior, Tsuta - Magnification is 13
When 111 turns seven times, Tsutashin 11 not only crystallizes, but also 18
The strong fIK-non-lightning IC of the dish that is deceptive becomes low.

かくして得られる不話性微粒子含有ポl:f−スプル繊
纏から、その一部′klk去するに&1必要に応じて*
m又は仮撚加工等を施した後、又番i更に布帛にした後
アルカリ化合物の水溶液でJll&瑠することkより容
易に行なうこ、とができる。
From the thus obtained non-talking fine particle-containing poly:f-sprue fiber, a portion of it is removed by &1 if necessary.
After the fabric has been subjected to a false twisting process or the like, it can be further made into a fabric and then washed with an aqueous solution of an alkali compound.

ここで使用するアルカリ化合物とし、てを1水酸化ナト
リウム、水酸化カリウム、テトラメチルアンモニウムノ
1イド−オキサイド、炭酸すFリウム、炭酸カリウム等
をあげるととbtできる。
The alkaline compounds used here include sodium monohydroxide, potassium hydroxide, tetramethylammonium oxide, sodium carbonate, potassium carbonate, and the like.

なかでも水酸化ナトリウム、水酸化カリウムb%特に好
ましい。
Among them, sodium hydroxide and potassium hydroxide (b%) are particularly preferred.

かかるアルカリ化合物の水11!1ins度tz、フル
カリ化合物の種類、M種条件等によって異なるが1通常
0.01〜40重量うの範囲b%好ましく、畳に0.1
〜SO重量囁の範囲が好まし−1゜J6瑠温度は常温〜
100℃の範回が好ましく、l&垣待時間1分〜4時間
のtsで通常行なわれる。また、このアルカリ化合物の
本**の4611によつ″Cs出―去する量は、繊維重
量に対し【2重量う以上の範IIKすべきである。この
よ5にアル、力替化合物の水**″em@することkよ
って、可III党線の波長よりも小さな凹凸を繊維表面
の童画に均−Ky/II威せしめることができ、前記し
た如き繊−内部の*aな高次微細構造を有する微孔性ポ
リエステル繊倫が得られ、通常のIm!麟構造を有する
同様の微孔性ポリエステル繊−に比較して染色した一改
善された色の深みと#−性を呈するよ5になる。
Although it varies depending on the water of the alkaline compound, the type of the alkaline compound, the M type conditions, etc., it is preferably in the range of 0.01 to 40% by weight, and 0.1% to the tatami mat.
~SO weight is preferably in the range of -1°J6 temperature is room temperature~
A temperature range of 100° C. is preferable, and it is usually carried out at a temperature of 1 minute to 4 hours. In addition, the amount of Cs removed by this alkaline compound according to Book ** 4611 should be in the range of 2 weight or more relative to the weight of the fiber. By applying water **''em@k, unevenness smaller than the wavelength of the normal line can be uniformly applied to the children's picture on the fiber surface, and the *a higher order inside the fiber as described above can be made uniform. A microporous polyester fiber with a microstructure is obtained, and the normal Im! Compared to similar microporous polyester fibers having a lint structure, the dyed product exhibits improved color depth and #5.

なお、本発明の方法により得られるポリエステルー−に
は、必l!に応じて任意の添加剤、例えば触S、着色防
止剤、耐11sam、螢光増日剤、艶11&錫0着色剤
等が食まれていてもよ一ゝ・ 以下に実施例をあげてglK1m!―する。*總例中の
部及びうは重量部及び重量%を示(、得られる一曽エス
テル繊膳t−m色したーの色の譲゛み。
In addition, the polyester obtained by the method of the present invention must have the following properties: Depending on the situation, optional additives such as GLK1M, anti-coloring agents, 11sam resistance, fluorescent sun increasing agents, gloss 11 & tin 0 colorants, etc. may be included.Examples are given below. ! -do. *Parts and weight percentages in the examples indicate weight parts and weight %.

摩擦変色は以下の方法で一定した拳 0) 色の痒み 色の灘みtsす尺度としては銀色[(K/8)を用いた
。この値はサンプル布の分tm射率(R)を島津RC−
14811記分光光度計にて調定し、次に示すクペルカ
ー^ンク(Kub@lKm −Mu n k )の式か
ら求める。この値が大きいはと衆色効果が大きいことを
示す。
Friction discoloration was determined using the following method. Silver color [(K/8) was used as the scale for the itchy color. This value calculates the tm emissivity (R) of the sample cloth by Shimadzu RC-
14811 using a spectrophotometer, and obtained from the following Kupelkerk equation (Kub@lKm - Mun k ). A large value indicates a large tortoise effect.

なお、区は徴収係数、8は散乱係数を示す。Note that ward indicates a collection coefficient and 8 indicates a scattering coefficient.

(■)  摩擦変色 摩msろう度試験用の学振履平面摩耗機を使用して、摩
擦布としてボ□エチレンテレフタレート100%からな
るジ曹−ゼットを用い、試験布な5ooJjの加重下で
所定l数平両摩耗して、変色の度合を変褪色用グレース
ケールで判定した。耐摩耗性が極めて低い場合t1ml
とL、極Toて14い場合’f:5InL4゜実用上4
#1以上が必要であA。
(■) Using a friction discoloration/friction failure test using a Gakusho flat wear machine, the friction cloth was made of dicarbonate made of 100% ethylene terephthalate, and the test cloth was subjected to a specified load of 50Jj. The degree of discoloration was determined using a gray scale for discoloration and fading. If wear resistance is extremely low, t1ml
and L, if the pole Tote is 14, 'f: 5InL4゜Practically 4
A: #1 or higher is required.

実線l1lt テレフタル酸ジメチル100I1.エチレンダ讐コール
611酢酸カルシク^1水塩・、0・郁(テレフタル酸
ジメチルに対して・、・6・士気下4時間かけて14番
℃から3sO℃まで昇温して生成するメタノールを系外
に留去しながらエステル交換反応な行なった。続いて得
らえた反応生成物に、予め@、 @ ill #′)l
ン酸ト讐メチルCテレフタル酸ジメチルに対して・、−
9sモル%)と0.31都の酢酸カルシウム1水塩(リ
ン酸トvメチルに@して1/8倍モル)と七S、S部の
エチレングリコール中で1s・℃の温度において食31
1流下−・分岡叉応せしめて゛調製した蓼ン酸ジエステ
ルカルシクム塩の透嘴濤IIl先31部に麿温下・、a
t@の跡aカルシウム1水塩(lン鐙ト曽メチルIC増
して・、I@4ル)を溶解姥しめて得た曽ン臆ジーステ
ルヵルシク!塩とlImカルシクムとの拠會透*S演9
.畠8部を添加し、次い″e二二酸化アンチン70.0
4g添加して重合伽に移した0次いで1111間かけて
1・・■HIから1■翼Iまで威圧し、同時E1時間3
・分かけて5uet:からsai℃まで昇温した。1箇
■・I以下の減圧下、重合温度8−1℃で更Km時間、
合計4時間SO分重合して極限粘度@、6IIs軟化点
*is’Cで不活性徽誼子(1,6%を含有するボVマ
ーを得た0反応終了後ポリマーを常法に’lllいチッ
プ化した。
Solid line l1lt Dimethyl terephthalate 100I1. Ethylene Daenicol 611 Calcium Acetate Monohydrate (for dimethyl terephthalate), 6. Raise the temperature from No. 14°C to 3sO°C over 4 hours under reduced pressure and remove the generated methanol from the system. A transesterification reaction was carried out while distilling off.Then, the reaction product obtained was preliminarily treated with @, @ill #')l
For dimethyl terephthalate, -
9 s mol%) and 0.31 molar calcium acetate monohydrate (1/8 times the mol in methyl phosphate) and 7 S, S parts at a temperature of 1 s/°C in ethylene glycol.
1st stream - 31 parts of the transparent beak IIl of the prepared diester calcicum salt of oxalic acid was mixed with water and heated under heat.
The traces of t@ were obtained by dissolving and steeping calcium monohydrate (I@4). The relationship between salt and lImcalcicum*S performance 9
.. 8 parts of Hatake was added, and then 70.0 parts of antithene dioxide was added.
Added 4g and transferred it to the polymerization cage. 0 then 1111 hours to intimidate from 1...■HI to 1■ wing I, and at the same time E1 hour 3
- The temperature was raised from 5uet: to sai°C over a period of minutes. Under reduced pressure of 1 part ■・I or less, at a polymerization temperature of 8-1°C for an additional Km time,
Polymerization was carried out in SO for a total of 4 hours to obtain an inert bomer with an intrinsic viscosity of 6IIs and a softening point of 1.6%. Made into chips.

このチップを常法により乾燥し、孔径・、1■の円形紡
糸孔を24個穿設した紡糸0門から、紡糸温度2mK’
C:、で濤−吐出し、口金直下で風速・、!Isa/秒
の冷却風により冷却固化させ、その後4!!410諺/
分の速度で引取り、ボビンに巻き取り、aSデニール、
切断伸度11%。
This chip was dried by a conventional method, and the spinning temperature was 2 mK' from a spinning hole in which 24 circular spinning holes with a hole diameter of .
C:, Discharge, wind speed directly below the nozzle...! Cool and solidify with cooling air at Isa/sec, then 4! ! 410 proverbs/
Pick up at a speed of 1 minute, wind on a bobbin, aS denier,
Cutting elongation 11%.

−次降伏強度6.−I JF/ dsでXe 4 @ 
% s ム0、0 ? m m 1M1& @、 @ 
!易の未蔦伸糸を得た6次いでこの未、蔦伸糸を非加熱
下で嶌伸倍率1.11倍で延伸し、1sデニール、切断
伸度10%。
-Yield strength6. -I JF/ds Xe 4 @
%smu0,0? m m 1M1& @, @
! 6 Next, the undrawn yarn was drawn at a stretching ratio of 1.11 times without heating to obtain a denier of 1 s and an elongation at break of 10%.

沸水収縮率a%の蔦伸蟲とした。It was made into a tsuta-shinmushi with a boiling water shrinkage rate of a%.

この蔦伸糸を(・経糸)撚数soo’r/M、書度40
本/3.(緯糸)OT/M、密度40本/傷で平織物に
製麺し五番。
The number of twists of this vine drawn thread (warp) is soo'r/M, and the writing speed is 40.
Book/3. (Weft) OT/M, density 40 threads/wound, made into plain woven fabric, No. 5.

得られた生機を當俵によりプリセッシ後、l繁の卒鐘化
す)−り^水s*”t’沸沸騰麦皮て一塩し、減量皐黛
・繁の布帛を得た。
The obtained greige fabric was precessed using a straw bale, and then boiled with water and salted to obtain a reduced-strength fabric.

この布帛をDIamix B1m@k KG−Pa (
ミ菱化威工業−製晶)1易囁・vfで凰3・℃で蟲・分
間染色後、水酸化ナトリウム*I/Iおよび^イドwt
ルファイトII/′lを含む水溶1mてテ・℃で20分
mm51e、洗浄して墨染布を得た。
This fabric is DIamix B1m@k KG-Pa (
Mitsubishi Kawei Industries - Seisatsu) After staining with 1 yen/vf for 3 min/min at ℃, sodium hydroxide*I/I and ^ide wt
The cloth was washed with 1 m of an aqueous solution containing ruphite II/'l at TE.degree. C. for 20 minutes to obtain an ink-dyed cloth.

この黒染布の色の深みおよび摩III s o I回後
の耐摩振蜜も性は第1表に示した過′りであった。
The depth of color and the abrasion resistance of this black dyed fabric after three cycles of polishing were as shown in Table 1.

実施例意 テレフタル酸ジメチル1・・郁、エチレング曽コール・
・都、酢酸カルシウム1水亀O,aS部をエステル交換
曽に仕込み、窒素ガス雰−気下4時間かけ″(14・℃
から意sO℃まで昇温して生成するメタノールを系外に
雷去りながらエステル交換反応な行なった。続いて得ら
れた反応−に、・、64部の一鐙讐チウム無水塩(テレ
フタル酸ジメチルに対して1. I畠毫ル%)を添細し
、このi分aX・、ss都の正ψン酸(テレフタル酸ジ
メチルに対して0.69モルラ)、WIK%分後KO,
64鶴の二酸化アンチモン@、64゜Sを添加して重合
缶に移した0次いでカチオン染料可染性共重合成分とし
てs、に−ジ(I−ヒト−キシエトキシカルボニル)ベ
ンゼンスルホン酸ナトリウA4.6部(テレフタル鹸ジ
メチルに対して:、sモル%)を重合薔に添加した。鏡
いて1時間かけて160■H1かも1−Hlまで減圧し
1.同時に1時間3.0分かけ? t S @ ’Ct
pも2IO℃まで昇温した。1■Hjl以■の減圧下、
Example: Dimethyl terephthalate 1... Iku, Ethylene Sokole...
・Pour 1 part of calcium acetate into a transesterification tank and heat it for 4 hours under a nitrogen gas atmosphere (14°C).
The transesterification reaction was carried out while the temperature was raised from 0°C to 50°C and the methanol produced was removed from the system. Subsequently, .64 parts of anhydrous lithium salt (1.1% based on dimethyl terephthalate) was added to the resulting reaction, and this i-minute aX. ψphosphoric acid (0.69 molar relative to dimethyl terephthalate), KO after WIK% min,
64 Tsuru's antimony dioxide@, 64°S was added and transferred to a polymerization vessel.Next, as a cationic dye-dyeable copolymerization component, sodium di-di(I-human-oxyethoxycarbonyl)benzenesulfonate A4. 6 parts (relative to dimethyl terephthalate: s mol %) were added to the polymerized rose. Look in the mirror and reduce the pressure to 160■H1 or 1-Hl over an hour.1. 1 hour and 3.0 minutes at the same time? t S @ 'Ct
p was also raised to 2IO°C. Under reduced pressure of 1 Hjl or less,
.

重合温度艷1℃で更に2時間目分、合計4時間重合し、
極限粘度@、11!、軟化点!ia℃のポリマーを得た
Polymerization was carried out for an additional 2 hours at a polymerization temperature of 1°C, for a total of 4 hours.
Intrinsic viscosity @, 11! , softening point! A polymer of ia°C was obtained.

とのボVマーな用いて、以下実施例1と同機に一遍紡糸
・冷延伸・II繊・プVゞット・7“カリ処壜な行なっ
て減量率!O%の平織物を得た。
Using the same machine as in Example 1, spinning, cold drawing, II fiber, pu-Vit, and 7" potash treatment were carried out using the same machine as in Example 1 to obtain a plain woven fabric with a weight loss rate of 0%. .

このアルカリ処理後の声帛をムla@a Catkll
・n111ack CD−GLH(保土谷化学■勇晶)
 I %ewfで芒硝z I / Iを會む*浴中にて
130℃で一@O分間染色後、常法に従ってンービング
を行ない墨染布を得た。この墨染布の色の深みおよび摩
耗20@■後の耐摩擦変色性は館1表に示した通りであ
った。
The voice after this alkali treatment is uneven @a Catkll
・n111ack CD-GLH (Hodogaya Chemical Yusho)
After dyeing in a bath containing Glauber's salt z I/I at 130°C for 1 minute, an ink-dyed cloth was obtained by annealing according to a conventional method. The color depth and abrasion discoloration resistance after abrasion 20@■ of this ink-dyed fabric were as shown in Table 1.

なお、ここで得られた未延伸糸はXs 37%。Note that the undrawn yarn obtained here had an Xs of 37%.

ム@、 @ ? @ *んa @、 02 mの微細構
造を有していた。
Mu@, @? It had a microstructure of @*na@, 02 m.

地較儒1 実施例lにおいて行なった高速紡糸、J’1駕伸に代え
て、引取り適度1 ’1”’OO”II 7分の通常の
゛紡糸と延伸温度ss℃で延伸倍率3.s倍の通常の延
伸を行なう以外は実施lfiと同様に行なつ得、以下実
施例1と岡@に行なって、減量重電O%の黒msを得た
Ground Comparison 1 Instead of the high-speed spinning and J'1 drawing carried out in Example 1, the take-up mode was 1'1'''OO''II, normal 'spinning for 7 minutes, and the stretching temperature was ss°C, and the draw ratio was 3. The same procedure as in Example 1 was carried out except that ordinary stretching was carried out by s times, and the same procedure as in Example 1 was carried out to obtain a black ms with a weight loss of 0%.

艙呆は第1表に示した通りであった。The swelling was as shown in Table 1.

比較儒舅 実施例!において行なった高速#系、冷蔦伸に代えて、
引取り適度11@0■/分の過電の紡糸と延伸温度si
’tで延伸倍率3.z倍の通常の延伸を行なう以外は実
施例3と同機に行なって1sデニール/24フイラメン
トの鷺伸蟲を得、以下11施例2と同機に行なって、減
量率30%の墨染布を得た。
Comparative Confucian example! In place of the high-speed # system and cold tsuta-shin that was done in
Over-current spinning and drawing temperature si with take-up mode of 11 @ 0 ■/min
Stretching ratio is 3. A 1s denier/24 filament Sagi-shinmushi was obtained by using the same machine as in Example 3, except for the normal stretching of z times. Ta.

結果は第1表に示した通りであった。The results were as shown in Table 1.

第  1  ・表Chapter 1/Table

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

る□ためのXIHI@強置―線であり、  leは結晶
によるa祈fifi、Iaは非晶による一Nm度を示す
。 手続補正書 昭和暴1年 4月 20日 特許庁長官殿 1、事件の表示 特願昭 @7     311311号2、発明の名称 ポリエステル4Il#11の製造法 3、補正をする者 事件との関係  特許出願人 大阪市東区南本町1丁目11番地 (300)帝人株式会社 代表者 徳 末 知 夫 (11羽細書第10][第1行に「シ地カゲル」とある
を「シリカゾル」と訂正する。 (!1 同第14頁第9行に「毫ル道」とあるを「セル
数」と訂正する。 (8)  同嬉11頁jlxt行〜第20行に「メチル
アSドホスフエーシ、エチルテ曙Vホスフェート、プ手
ルアIFホスフェート」とあるを「エチルアシドホスフ
ェート、エチルアシドホスフェート、ブチルアシVホス
フエーシ」と訂正すゐ。 (4)同第!3貰第20行にr (t+nfsid1n
g ) Jとあるをr (unfoldlmg ) J
と訂正する。 (5)  同第24頁第14行に「複纏祈皐」とあるな
rlIfR車」と訂正する。 (61同第33頁第11行に「金#l癒下−O分関又応
」とあるをr全還流下60分間反応」と訂正する。 以  上
It is the XIHI@forced line for □, where le indicates a fifi due to crystal, and Ia indicates 1 Nm degree due to amorphous. Procedural Amendment Written April 20, 1927, Mr. Commissioner of the Japan Patent Office 1, Indication of Case Patent Application Showa @ 7 311311 No. 2, Name of Invention Process for Manufacturing Polyester 4Il #11 3, Person Making Amendment Relationship with Case Patent Applicant: 1-11 Minamihonmachi, Higashi-ku, Osaka (300), Teijin Ltd. Representative Tomoo Tokusue (11 Specification No. 10) [Correct the phrase "Sijikagel" in the first line to read "Silica Sol." (!1 In the same page, page 14, line 9, the word “mall road” is corrected to “the number of cells.” , Putelua IF phosphate" has been corrected to "ethyl acid phosphate, ethyl acid phosphate, butyl acid V phosphate". (4) Same as above! In the 20th line of the 3rd line, r (t+nfsid1n)
g) J and aruwo r (unfoldlmg) J
I am corrected. (5) On page 24, line 14 of the same page, it is corrected to read ``completion prayers''. (In 61, page 33, line 11, the text ``Gold #l cured - O-branch mater reaction'' is corrected to read ``R reaction for 60 minutes under total reflux.'')

Claims (1)

【特許請求の範囲】 平均の一次着子僅が1@@111ターン未−である不活
性徽曽子を0.1〜2重量弊會有り。 該不”活性黴曽子は1・・々す1タ一ン以上の下記で定
義する二次凝Jl諺子が繊維横断画1・雫方々ターン当
り3儒以上存在しない不活性徴曽子含有ポリエステル鎗
織であって鍍繊錨食体つ複1折ムfiLO,@1740
,14 、非晶領域の複履析ΔlがOo・6以下で且つ
曽蟲化jIx@がl@%以上のポリエステル未駕伸繊膳
を非加熱状態で1.01〜t、S、 S普に蔦伸し、し
かる後アルカリ感看することによって鍍繊維の少な(と
も3重量弊を溶出せしめることを畳黴とするポリエステ
ル繊維の製造法、    ・ 但し、二次凝錫曽子とは一次曽子iが職制で會るS*に
拡大された電子■黴鏡写真で克て、隣鋳する一次着子の
中心間層−が一次曽子直径の3普秦−#cIII遮り舎
った状■の曽子群をいう。
[Claims] We have an inert wafer with a weight of 0.1 to 2, whose average primary bond is only 1 @ 111 turns. The inert molten powder contains an inert molten powder that does not have a secondary stiffness defined below of 1 ton or more per fiber cross-stroke or 3 or more drops per turn. Polyester woven fabric with sewage anchor and two folds fiLO, @1740
, 14, a polyester unstretched fiber sheet in which the compound analysis Δl of the amorphous region is Oo・6 or less and the intensification jIx@ is 1@% or more is heated from 1.01 to t, S, S in a non-heated state. A method for manufacturing polyester fibers in which the tatami mold is made by stretching the vines and then exposing them to alkali to elute the 3 weight atom of the fibres. Electron magnified to S* where child i meets in the office ■ Overcame with mold mirror photograph, central interlayer of primary cladding next to cast - 3 pieces of diameter of primary soshi - #cIII intercepted state ■It refers to the Soshi group.
JP3936682A 1982-03-15 1982-03-15 Preparation of polyester fiber Granted JPS58163718A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3936682A JPS58163718A (en) 1982-03-15 1982-03-15 Preparation of polyester fiber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3936682A JPS58163718A (en) 1982-03-15 1982-03-15 Preparation of polyester fiber

Publications (2)

Publication Number Publication Date
JPS58163718A true JPS58163718A (en) 1983-09-28
JPS641583B2 JPS641583B2 (en) 1989-01-12

Family

ID=12551055

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3936682A Granted JPS58163718A (en) 1982-03-15 1982-03-15 Preparation of polyester fiber

Country Status (1)

Country Link
JP (1) JPS58163718A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6163706A (en) * 1984-09-05 1986-04-01 Teijin Ltd Method of melt spinning
JPS61239016A (en) * 1985-04-17 1986-10-24 Teijin Ltd Production of ultrafine fiber

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55107544A (en) * 1979-02-08 1980-08-18 Kuraray Co Gloss improved polyester knitted fabric and method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS55107544A (en) * 1979-02-08 1980-08-18 Kuraray Co Gloss improved polyester knitted fabric and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6163706A (en) * 1984-09-05 1986-04-01 Teijin Ltd Method of melt spinning
JPH028042B2 (en) * 1984-09-05 1990-02-22 Teijin Ltd
JPS61239016A (en) * 1985-04-17 1986-10-24 Teijin Ltd Production of ultrafine fiber
JPH049206B2 (en) * 1985-04-17 1992-02-19

Also Published As

Publication number Publication date
JPS641583B2 (en) 1989-01-12

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