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JPS63282308A - Production of water-soluble crimped vinylon - Google Patents

Production of water-soluble crimped vinylon

Info

Publication number
JPS63282308A
JPS63282308A JP11695487A JP11695487A JPS63282308A JP S63282308 A JPS63282308 A JP S63282308A JP 11695487 A JP11695487 A JP 11695487A JP 11695487 A JP11695487 A JP 11695487A JP S63282308 A JPS63282308 A JP S63282308A
Authority
JP
Japan
Prior art keywords
temperature
water
vinylon
fiber
yarn
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP11695487A
Other languages
Japanese (ja)
Inventor
Masahiko Okubo
大久保 昌彦
Takaaki Sugishita
杉下 高昭
Shirou Suzuki
鈴木 師朗
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.)
NICHIBI KK
Original Assignee
NICHIBI KK
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 NICHIBI KK filed Critical NICHIBI KK
Priority to JP11695487A priority Critical patent/JPS63282308A/en
Publication of JPS63282308A publication Critical patent/JPS63282308A/en
Pending legal-status Critical Current

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  • Artificial Filaments (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

Abstract

PURPOSE:To easily obtain the titled fiber having excellent crimping property, on an industrial scale at a low cost, by subjecting an undrawn vinylon fiber successively to heat-treatment and drawing treatment at respective specific temperature and carrying out crimp-developing treatment of the resultant latent crimping fiber in a specific atmosphere. CONSTITUTION:A polyvinyl alcohol used as a raw material is extruded from a spinneret by dry-spinning process. The obtained fiber is heat-treated at a temperature higher than the drawing temperature by >=60 deg.C and within 120-230 deg.C and then drawn at a temperature lower than the above heat- treatment temperature by >=60 deg.C and within 20-150 deg.C. The obtained latent crimping fiber is treated in a steam atmosphere of RH 70-100%, in water or in a hot dry atmosphere of 120-230 deg.C to develop the crimp and obtain the objective fiber.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は工業的に有利な水溶性巻縮ビニロンの製造法で
あり、更に詳しくは乾式紡糸法における水溶性ビニロン
に対する巻縮付与に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an industrially advantageous method for producing water-soluble crimped vinylon, and more specifically relates to imparting crimping to water-soluble vinylon in a dry spinning method. be.

〔従来の技術〕[Conventional technology]

水溶性ビニロンは、その特徴を生かして各種産業分野に
利用されまた利用のための研究が行なわれている。繊維
分野への応用例としては、水溶性ビニロンと各種の繊維
を混紡、交織し、最終製品とするまでの適当な加工段階
で水溶性ビニロンを俗解除去することによって最終製品
の付加価値を高める使用法がある。か\る分野では、工
業的に安価で容易に水溶性ビニロンに巻縮を付与するこ
とができれば最終製品価値の大幅な向上、並びに利用範
囲の拡大が図れる等その意義は大きい。
Water-soluble vinylon is used in various industrial fields by taking advantage of its characteristics, and research is being conducted for its use. An example of its application in the textile field is to increase the added value of the final product by blending and weaving water-soluble vinylon with various fibers and removing the water-soluble vinylon at an appropriate processing stage before making the final product. There is a usage. In these fields, if crimping could be applied to water-soluble vinylon easily and inexpensively on an industrial scale, it would be of great significance, as it would greatly improve the value of the final product and expand the scope of its use.

従来の巻縮ビニロンの製造法としては、例えば紡糸時に
低温延伸で内部歪を太きくシ、アセタール化処理等によ
り巻縮を発現させる方法、或は特公昭43−26349
号、同44−2071号、同44−2507号、同44
−2508号等のように、糸条中の二成分の収縮差を利
用して巻縮を発現させる方法、又はウーリー加工、ニッ
トデニソト法等が提案されている。
Conventional methods for producing crimped vinylon include, for example, increasing the internal strain by low-temperature stretching during spinning, or developing crimping by acetalization treatment, or
No. 44-2071, No. 44-2507, No. 44
There have been proposed methods such as No. 2508, which utilize the difference in shrinkage between two components in the yarn to produce crimp, wooly processing, knit Denisoto method, and the like.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながらこれらの方法は、いずれも複雑な製造設備
や装置が必要であり、その結果コスト高を招くため、工
業的に不利であり、前述のような目的には経済上好まし
くなく一部の限られた耐熱水性の高いビニロンに応用さ
れているにすぎない。
However, all of these methods require complicated manufacturing facilities and equipment, resulting in high costs, and are therefore industrially disadvantageous. It is only applied to vinylon, which has high hot water resistance.

そこで本発明者らは先に特願昭61−45180号、同
61−45181号等により工業的に容易な水溶性巻縮
ビニロンの製造法を提案したが、連続操業性等の面でな
お改良の余地があった。
Therefore, the present inventors have previously proposed an industrially easy method for producing water-soluble crimped vinylon in Japanese Patent Application Nos. 61-45180 and 61-45181, etc., but improvements still need to be made in terms of continuous operability, etc. There was room for.

か\る現状にかんがみ、工業的に安価、容易にかつ高性
能の巻縮を有する水浴性巻縮ビニロンを製造する方法に
ついて鋭意研究した結果、本発明を完成したものである
In view of the current situation, the present invention was completed as a result of intensive research into a method for industrially producing water-bathable crimped vinylon that is inexpensive, easy, and has high performance crimping.

〔問題点を解決するための手段〕[Means for solving problems]

すなわち本発明においては、乾式紡糸法によシ水溶性巻
縮ビニロンを製造する際、通常の紡糸技術において慣用
されている常識的工程である延伸→熱処理なる工程順を
とること々く、特定の制限された範囲で、逆に先ず熱処
理を行ない、次に延伸工程にかけるという順序で行なう
ことにより、潜在巻縮^、次いでこの潜在巻縮糸に対し
特定条件下で巻縮発現処理を行なうことを大きな特徴と
するものである。このように行なうことにより工業的に
極めて安価に、かつ容易に、水中溶解度の異なる各種水
容性ビニロンに対し、高性能の巻縮を効率よく付与させ
ることができ六ものである。
That is, in the present invention, when producing water-soluble crimped vinylon by the dry spinning method, the process sequence of drawing → heat treatment, which is a common process commonly used in ordinary spinning technology, is often used, and specific steps are taken. Within a limited range, by first performing heat treatment and then subjecting it to a drawing process, latent crimp is achieved, and then this latent crimp yarn is subjected to crimp development under specific conditions. This is a major feature. By carrying out this method, it is possible to efficiently impart high-performance crimp to various water-soluble vinylons having different solubility in water, industrially at extremely low cost and easily.

すなわち本発明の要旨とするところは、ポリビニルアル
コールを原料として乾式紡糸法により、水溶性巻縮ビニ
ロンを製造するに際し、延伸前に下記条件を満足する温
度(Tj)にて熱処理を施し、然る後に、該条件を満足
する温度(T2)にて延伸処理を施すことにより、潜在
巻縮糸を得た後、該潜在巻縮糸i R−H70〜100
%の水蒸気雰囲気もしくは水中又は120〜230℃の
乾熱雰囲気にて処理し、巻縮を発現させることを特徴と
する水容性巻縮ビニロンの製造法であって、温度条件は
、T1)T2+60C℃)   且っ 2 3 0>T、)120(1:I L  50>T2>20i℃+ である。
That is, the gist of the present invention is that when producing water-soluble crimped vinylon by dry spinning using polyvinyl alcohol as a raw material, heat treatment is performed at a temperature (Tj) that satisfies the following conditions before stretching. Later, by performing a drawing process at a temperature (T2) that satisfies the conditions, a latent crimped yarn is obtained, and then the latent crimped yarn i R-H70-100
% of water vapor atmosphere or water or a dry heat atmosphere of 120 to 230°C to develop water-soluble crimped vinylon, the temperature conditions are T1) T2 + 60C. ℃) and 2 3 0>T, ) 120 (1:I L 50>T2>20i℃+.

次に、本発明について更に具体的に詳しく説明する。Next, the present invention will be explained in more detail.

水溶性巻縮ビニロンの原料としては、公知のポリビニル
アルコール(以下PVAと略す)が利用出来るが、ケン
化度88モルチ以上、重合度800〜1700程度のも
のが好ましい。又、変性PVA 、例エバ、マレイン酸
、或いは、インプロペニルアセテート等と共重合させて
、ケン化した、変性度2〜15モルチ程度の結晶阻害基
を有するものでもよい。
As a raw material for water-soluble crimped vinylon, known polyvinyl alcohol (hereinafter abbreviated as PVA) can be used, but those having a degree of saponification of 88 molti or more and a degree of polymerization of about 800 to 1,700 are preferred. It may also be a modified PVA, such as one copolymerized with Eva, maleic acid, impropenyl acetate, etc., and saponified to have a crystal-inhibiting group with a degree of modification of about 2 to 15 mol.

原液の作製は、公知の方法に準ずればよく、原料を加熱
浴解させ、濃度28.〜37チ、粘度100〜700ポ
イズ程度に調整すればよい。該原液中への、少量の添加
剤(消泡剤、曳糸性向上剤等)の混合は、差しつかえ々
い。
The stock solution may be prepared according to a known method, and the raw material is dissolved in a heating bath to a concentration of 28. The viscosity may be adjusted to about 100 to 700 poise. Mixing a small amount of additives (antifoaming agent, stringiness improver, etc.) into the stock solution is not a problem.

次に、本発明の特徴の1つである、乾式紡糸条件につい
て述べる。
Next, dry spinning conditions, which are one of the features of the present invention, will be described.

PVA原液を、公知のギャーポンゾ及びノズルにより、
乾式紡糸筒内へ押し出して後、通常は、延伸ロールによ
り、延伸処理を経てから、熱処理ロールにより、熱処理
操作が行われるが、該方法では、通常、延伸温度より熱
処理湿度の方が高い為、繊維構造的に、安定化或いは、
均質化される方向となり、本発明の目的とする潜在巻縮
性の付与という点からは、不利な傾向にあることを見出
した。
PVA stock solution is mixed with a known Gya Ponzo and nozzle.
After being extruded into a dry spinning tube, it is usually subjected to a stretching process using a stretching roll, and then a heat treatment operation is performed using a heat treatment roll, but in this method, the heat treatment humidity is usually higher than the stretching temperature. In terms of fiber structure, stabilization or
It has been found that this tendency tends to be homogenized, which is disadvantageous in terms of imparting latent crimpability, which is the objective of the present invention.

本発明の目的達成の為には、先づ未延伸の状態で、糸条
化されつ\ある過程で熱処理効果を与えて、繊維構造を
一時的に安定化させた後に、熱処理時の温度よりも低温
で延伸効果を与えることにより、製品糸として要求され
る物性を維持する範囲で、繊維構造を、物理的、機械的
に乱すことにより、効果的に潜在巻縮性能を付与させ得
ることを見出したのである。
In order to achieve the purpose of the present invention, firstly, in an undrawn state, the fiber structure is temporarily stabilized by applying a heat treatment effect during the process of being turned into yarn, and then the temperature at the time of heat treatment is lowered. It has been shown that latent crimp performance can be effectively imparted by physically and mechanically disturbing the fiber structure within a range that maintains the physical properties required for product yarn by applying a stretching effect at low temperatures. I found it.

この際、熱処理温度(TIJと、延伸温度(T2)は、
以下の条件を満足することが必須である。
At this time, the heat treatment temperature (TIJ) and the stretching temperature (T2) are
It is essential to satisfy the following conditions.

TI >T2+60 (℃l   且つ230>TI>
120F℃ 1 1 50 >T2>20 I ℃+ 即ち、T1がT2より、60℃以上高いことが必要であ
り、(T1−T2)が60℃以内となると、良好な潜在
巻縮能の付与が困難、若しくは不可能となる。
TI > T2 + 60 (℃l and 230 > TI >
120F℃ 1 1 50 >T2>20 I℃+ In other words, T1 needs to be higher than T2 by 60℃ or more, and if (T1-T2) is within 60℃, good latent curling ability cannot be imparted. becomes difficult or impossible.

t’r1−’r2+は、好ましくは70℃以上、更に好
ましくは80℃以上であれば、優れた潜在巻縮能を有す
る、水溶性ビニロンが得られる。
When t'r1-'r2+ is preferably 70°C or higher, more preferably 80°C or higher, a water-soluble vinylon having excellent latent crimp ability can be obtained.

T1は、2.30>T1>120に’C)の範囲とする
ことが肝要であり、好ましくは、220>TI>130
MCJである。T1は、使用されるPVAの種類、紡糸
速度、及び製品糸に要求される性能の一つである。水中
浸漬、処理時の溶解温度等との関連で、適宜決定される
ものであるが、230℃以上では、糸状の着色化、融着
化、等の問題が生じ、120℃以下では、熱処理効果に
よる一時的な繊維構造の安定化を付与する上で不充分と
なる。
It is important that T1 is in the range of 2.30>T1>120, preferably 220>TI>130.
It is MCJ. T1 is one of the characteristics required for the type of PVA used, the spinning speed, and the product yarn. It is determined as appropriate in relation to the melting temperature during immersion in water and treatment, but at temperatures above 230°C, problems such as filamentous coloration and fusion will occur, and below 120°C, the heat treatment effect will be reduced. This is insufficient to provide temporary stabilization of the fiber structure.

一方、T2は、150〉T2ン20(℃Mの範囲とする
ことが肝要であり、好ましくは、140>T2>30f
℃lである。
On the other hand, it is important that T2 is in the range of 150>T2>20(℃M, preferably 140>T2>30f
℃l.

熱処理工程で形成された、一時的に安定な繊維内結晶構
造を、製品糸として要求される繊維性能を維持させる範
囲で、物理的、機械的に乱すことにより、潜在的巻縮能
を付与させるものであり、150℃以上、又は、20℃
以下では、この潜在的巻縮能付与効果が乏しくなるか、
全く消滅するに至る。更に、必要な繊維性能が得られな
くなる場合もでてくる。
By physically and mechanically disturbing the temporarily stable intrafiber crystal structure formed in the heat treatment process within the range that maintains the fiber performance required as a product yarn, potential crimp ability is imparted. 150℃ or higher or 20℃
In the following, this potential curling ability imparting effect becomes poor, or
It ends up completely disappearing. Furthermore, there may be cases where the required fiber performance cannot be obtained.

延伸工程では、延伸倍率の特定が重要であるが、これは
、T1.T2.並びに製品糸に要求される、強伸度等の
繊維物性との相関により、2〜8倍の範囲で適宜選定さ
れる。
In the stretching process, it is important to specify the stretching ratio, which is determined by T1. T2. In addition, it is appropriately selected in the range of 2 to 8 times depending on the correlation with the fiber physical properties such as strength and elongation required for the product yarn.

熱処理工程で付与された一時的な繊維構造の安定性を延
伸効果により、繊維としての物性を維持させる範囲で乱
れさせる為には、熱処理時における温度効果を、延伸領
域に迄、波及させないことが有効であり、この目的の為
に工業的な連続工程では熱処理部と延伸部の境界に糸条
における熱の移動を阻止させる如き治具を、設置するこ
とは、本発明の遂行に大きく寄与する。
In order to disturb the temporary stability of the fiber structure imparted in the heat treatment process by the stretching effect to the extent that the physical properties of the fiber are maintained, it is necessary to prevent the temperature effect during the heat treatment from spreading to the stretching region. It is effective, and for this purpose, in an industrial continuous process, installing a jig that prevents the transfer of heat in the yarn at the boundary between the heat treatment section and the drawing section will greatly contribute to the accomplishment of the present invention. .

この目的に沿うものとして、ローラ、ピン、ガイド等が
好ましく用いられ、紡出糸条の繊度、速度、及び要求さ
れる巻縮性能(クリンプの数、山と谷の高さの程度ン等
により、形状、大きさ、材質、角度、等が適宜選定され
る。
For this purpose, rollers, pins, guides, etc. are preferably used, and depending on the fineness of the spun yarn, speed, and required crimp performance (number of crimps, degree of peak and valley height, etc.) , shape, size, material, angle, etc. are selected as appropriate.

以上の如くして、優れた潜在巻縮性能を有する水溶性ビ
ニロン糸条が得られる。
In the manner described above, a water-soluble vinylon yarn having excellent latent crimp performance can be obtained.

かくして得られた、高性能の潜在巻縮性を有する水溶性
ビニロン糸条を得ても、続いて行われる巻縮発現処理が
適切でなければ、目的とする高性能水溶性巻縮ビニロン
が、全く得られないか、若しくは、その巻縮性能の劣っ
たものとなる。
Even if a water-soluble vinylon yarn with high performance latent crimp properties is obtained in this way, if the subsequent crimp development treatment is not appropriate, the desired high performance water-soluble crimp vinylon will not be produced. Either it cannot be obtained at all, or its crimp performance is poor.

巻縮発現の機構は定かではないが、該潜在巻縮性を有す
る糸条を、制限された特定の雰囲気中に置くことにより
糸条の弛緩過程で巻縮が発現すること\なる。該巻縮発
現処理において、収縮を規制すると、巻縮の発現が困難
となることから、張力下での該処理は不利な条件となり
、通常は、2η/d以下の張力で行われる。
Although the mechanism by which crimping occurs is not clear, by placing the yarn with the latent crimping property in a specific, restricted atmosphere, crimping occurs during the relaxation process of the yarn. In the crimp development treatment, if contraction is restricted, it becomes difficult to develop crimp, so the treatment under tension is disadvantageous, and is usually carried out at a tension of 2η/d or less.

巻縮発現処理は、湿熱(水蒸気)法、乾熱法、何れも可
能であるが、原料PVAの種類(ケン化度、結晶阻害基
の有無、変性度、等ン及び紡糸条件、等によって、最適
処理温度が異ってくる。
Both wet heat (steam) method and dry heat method can be used for crimping, but depending on the type of raw material PVA (degree of saponification, presence or absence of crystal inhibiting groups, degree of modification, etc., spinning conditions, etc.) The optimum processing temperature varies.

湿熱法による巻縮発現処理では、湿度の管理が重要であ
り、密閉容器を使用して、RbH70〜100チ、好ま
しくは、R’争…80〜100%の高湿度雰囲気、若し
くは水中浸漬により行われる。R−H70チ以下では、
巻縮発現程度が不充分か、或いは全く巻縮が発現しなく
なる。水中浸漬の場合は、浴比に影響されず、通常の水
道水、或いは、イオン交換水等が使用出来る。水中溶解
温度の低い潜在巻縮ビニロンに対しては、水中浸漬法に
よる巻縮発現処理は不向きである。
In the curling development treatment by the wet heat method, humidity control is important, and the treatment is carried out using a closed container in a high humidity atmosphere with RbH of 70 to 100%, preferably R' of 80 to 100%, or by immersion in water. be exposed. For R-H70 or less,
The degree of crimping is insufficient, or crimping does not occur at all. In the case of immersion in water, normal tap water, ion exchange water, etc. can be used without being affected by the bath ratio. For latent crimp vinylon, which has a low dissolution temperature in water, crimp development treatment by dipping in water is not suitable.

湿熱法における巻縮発現処理時の温度及び時間について
例示すると、ケン化度95モルチ以上の糸条や、変性度
2〜8モルチ程度の糸条等では、50−95℃が好まし
く、ケン化度88モルチ程度の糸条や、マレイン酸、或
いはインプロペニルアセテート等で変性した変性度12
〜15モルチ程度の糸条では20〜50℃が適当である
。この際の処理時間は1〜60分間であり、湿度及び処
理量等との関連で、適宜選定される。
To give an example of the temperature and time during crimp development treatment in the moist heat method, for yarns with a degree of saponification of 95 molts or more, yarns with a degree of modification of about 2 to 8 molts, etc., the temperature is preferably 50-95°C; Modification degree 12 modified with threads of about 88 molti, maleic acid, impropenyl acetate, etc.
A temperature of 20 to 50°C is appropriate for yarns of about 15 to 15 molar. The processing time at this time is 1 to 60 minutes, and is appropriately selected in relation to humidity, processing amount, etc.

乾熱法による、巻縮発現処理は、120〜230℃好ま
しくは、130〜220℃の乾熱中にて、5分以内の短
時間にて行われ、ノ々ツチ法、連続法、何れも可能であ
る。230℃以上では、糸条の巻縮発現は良好となるが
、風合硬化、着色化、融着化等の問題が生じ、120℃
以下では、巻縮発現の程度が不充分となる。
The shrinkage development treatment by dry heat method is carried out in dry heat at 120 to 230°C, preferably 130 to 220°C, for a short time of 5 minutes or less, and both Nototsuchi method and continuous method are possible. It is. At temperatures above 230°C, the curling and shrinkage of the yarn is good, but problems such as hardening of the texture, coloration, and fusion occur.
Below this, the degree of curling will be insufficient.

湿熱法、乾熱法、何れも適切な湿度、或いは温度範囲を
外れると、優れた巻縮発現が不能となっタリ、糸条の接
着、融着、異常収縮等音引き起す。
In either the wet heat method or the dry heat method, if the humidity or temperature is outside the appropriate range, excellent crimping cannot be achieved, causing noises such as tapping, thread adhesion, fusion, and abnormal shrinkage.

以上、詳述した如く、本発明によシ、工業的に安価、容
易に、高性能水容性巻縮ビニロンを製造することが出来
、他繊維との併用により、付加価値の高い製品を製造す
ることが可能となる。
As detailed above, according to the present invention, high-performance water-soluble crimped vinylon can be produced industrially at low cost and easily, and when used in combination with other fibers, products with high added value can be produced. It becomes possible to do so.

以下に、実施例及び比較例を挙げて、本発明を具体的に
説明する。
The present invention will be specifically explained below by giving Examples and Comparative Examples.

実施例1 平均重合度1200.ケン化度99.5モル係のPVA
を使用して33重量%の水溶液を作製し、乾式紡糸法に
て紡糸口金より押し出し糸条を得た。
Example 1 Average degree of polymerization 1200. PVA with saponification degree of 99.5 molar
A 33% by weight aqueous solution was prepared using the following methods, and a yarn was extruded from a spinneret using a dry spinning method.

続いて熱処理温度200℃、延伸温度1oo℃とし、熱
処理ローラーと延伸ローラーの間にガイドを糸条進行方
向と45度の角度で設置し、糸条をガイドに巻きつけて
速度500m/分にて走行させて熱処理、延伸処理を行
なった。かくして、延伸倍率4倍、t 20d/30f
の潜在巻縮糸を得た。
Subsequently, the heat treatment temperature was set to 200°C, and the drawing temperature was set to 100°C. A guide was installed between the heat treatment roller and the drawing roller at an angle of 45 degrees to the yarn traveling direction, and the yarn was wound around the guide at a speed of 500 m/min. It was run and subjected to heat treatment and stretching treatment. Thus, the stretching ratio is 4 times, t 20d/30f
A latent crimped yarn was obtained.

次いでこの潜在巻縮糸上20℃の水道水中に1分間浸漬
した後、遠心脱水機にて含水率80%まで脱水した後、
50℃の熱風乾燥機中で乾燥し、水溶性巻縮ビニロン全
作製した。
Next, this latent crimped yarn was immersed in tap water at 20°C for 1 minute, and then dehydrated to a water content of 80% in a centrifugal dehydrator.
It was dried in a hot air dryer at 50°C to produce a water-soluble crimped vinylon.

比較例1 熱処理温度を200℃、延伸温度を160℃としたこと
以外は、実施例1と全く同じ条件で、水溶性巻縮ビニロ
ン全作製した。
Comparative Example 1 A water-soluble crimped vinylon was entirely produced under the same conditions as in Example 1, except that the heat treatment temperature was 200°C and the stretching temperature was 160°C.

実施例2 実施例1にて得た、潜在巻縮糸を収束して75■にカッ
トした後、無張力下にて、R−H95%温度90℃のス
チーム・ゼックスで5分間処理し、風乾して、水溶性巻
縮ビニロンを作製゛シた。
Example 2 The latent crimped yarn obtained in Example 1 was converged and cut into 75 squares, then treated with R-H 95% Steam ZEX at a temperature of 90°C for 5 minutes without tension, and air-dried. Then, water-soluble crimped vinylon was produced.

比較例2 実施例1にて得た、潜在巻縮糸を収束して75■にカッ
トした後、無張力下にて、R−H50%温度90℃のス
チーム・ゼックスで5分間処理し、風乾して、水溶性巻
縮ビニロン全作製した。
Comparative Example 2 After converging the latent crimped yarn obtained in Example 1 and cutting it into 75 cm, it was treated with Steam ZEX of 50% R-H and a temperature of 90°C for 5 minutes without tension, and then air-dried. A whole water-soluble crimped vinylon was prepared.

実施例3 インプロペニルアセテート全tt、sモルチ共重合させ
た後99モルチケン化した変性PVA (平均重合度1
100、変性度12.5モル%)を使用して、35重量
%の水溶液とし、乾式紡糸法にて紡糸口金より押し出し
、糸条を得た。
Example 3 Modified PVA (average degree of polymerization 1
100, modification degree 12.5 mol%) to make a 35% by weight aqueous solution, which was extruded from a spinneret by a dry spinning method to obtain yarn.

続いて熱処理温度130℃、延伸温度50℃とし、熱処
理ローラーと延伸ローラーの間にローラー’r糸条進行
方向と30度の゛角度で設置し、糸条をローラーに巻き
つけて速度400m1分にて走行させて熱処理、延伸処
理を行なつ念。かくして延伸倍率5.5倍、120d/
30fの潜在巻縮糸を得念。
Subsequently, the heat treatment temperature was set to 130°C, and the drawing temperature was set to 50°C. A roller was placed between the heat treatment roller and the drawing roller at an angle of 30 degrees to the yarn traveling direction, and the yarn was wound around the roller at a speed of 400 m/min. Please be sure to run the film for heat treatment and stretching. Thus, the stretching ratio is 5.5 times, 120 d/
A 30f latent crimped yarn is considered.

次いでこの潜在巻縮糸を無緊張下にて、210℃の熱風
乾燥機中で5秒間処理して水溶性巻縮ビニロンを作製し
た。
Next, this latent crimped yarn was treated in a hot air dryer at 210° C. for 5 seconds under no tension to produce water-soluble crimped vinylon.

比較例3 熱処理温度を130℃、延伸温度を110℃としたこと
以外は、実施例3と全く同じ条件で水溶性巻縮ビニロン
を作製した。
Comparative Example 3 A water-soluble crimped vinylon was produced under exactly the same conditions as in Example 3, except that the heat treatment temperature was 130°C and the stretching temperature was 110°C.

以上の実施例、比較例から得られた試料についての性状
評価結果を次表に示す。
The property evaluation results for the samples obtained from the above Examples and Comparative Examples are shown in the following table.

(表)  水溶性巻縮ビニロンの性状 ※1. 巻縮数は、10回測定の平均値、※2. 高さ
は、クリンプの山と谷の高さを測定した値、10回測定
の平均値、 ※3. 収縮率は、巻縮発現処理におけるもの。
(Table) Properties of water-soluble crimped vinylon *1. The number of curls is the average value of 10 measurements, *2. The height is the measured value of the peak and valley heights of the crimp, the average value of 10 measurements, *3. The shrinkage rate is based on the curling process.

上表に示した如く、実施例で得られた水溶性巻縮ビニロ
ンは、巻縮性能、特にクリンプの山と谷の高さが大きく
、優れたものであった。実施例2で得られたものは、梳
毛糸、或いは、紡毛糸等との混紡性がすこぶる良好であ
り、付加価値の高い加工糸の得られることが認められ念
As shown in the table above, the water-soluble crimped vinylon obtained in the Examples had excellent crimping performance, especially the height of the crimp peaks and troughs. The material obtained in Example 2 had very good blendability with worsted yarn or woolen yarn, and it was confirmed that a processed yarn with high added value could be obtained.

〔発明の効果〕〔Effect of the invention〕

以上の結果からも明らかなとおり、本発明の方法によれ
ば、各種水容性ビニロンに容易に巻縮性を付与でき、特
に水中溶解湿度の高い水溶性ビニロンに対して巻縮性能
(特にクリンプ部の山と谷の高さ]の点で優れた水溶性
巻縮ビニロンを、連続操業によって容易に効率よく製造
することができる。
As is clear from the above results, according to the method of the present invention, crimpability can be easily imparted to various types of water-soluble vinylon. A water-soluble crimped vinylon excellent in terms of peak and valley height can be easily and efficiently produced by continuous operation.

また得られた巻縮ビニロンは梳毛糸又は紡毛糸との混紡
性がよく繊維産業分野における各種の利用、応用範囲の
拡大が可能となり、その効果は極めて大きいものである
In addition, the obtained crimped vinylon has good blendability with worsted yarn or woolen yarn, making it possible to use it in various ways and expand the range of applications in the textile industry, and its effects are extremely large.

Claims (1)

【特許請求の範囲】 ポリビニルアルコールを原料として乾式紡糸法により、
水溶性巻縮ビニロンを製造するに際し、延伸前に、下記
条件を満足する温度(T_1)にて熱処理を施し、然る
後に該条件を満足する温度(T_2)にて延伸処理を施
すことにより、潜在巻縮糸を得た後、該潜在巻縮糸をR
・H70〜100%の水蒸気雰囲気もしくは水中又は1
20〜230℃の乾熱雰囲気にて処理し、巻縮を発現さ
せることを特徴とする水溶性巻縮ビニロンの製造法。 T_1>T_2+60(℃)且つ 230>T_1>120(℃) 150>T_2>20(℃) 但しT_1・・・熱処理温度 T_2・・・延伸温度
[Claims] By dry spinning method using polyvinyl alcohol as a raw material,
When producing water-soluble crimped vinylon, before stretching, heat treatment is performed at a temperature (T_1) that satisfies the following conditions, and then by stretching treatment at a temperature (T_2) that satisfies the conditions. After obtaining the latent crimped yarn, the latent crimped yarn is R
・H70-100% steam atmosphere or water or 1
A method for producing water-soluble crimped vinylon, which comprises treating it in a dry heat atmosphere at 20 to 230°C to develop crimping. T_1>T_2+60(°C) and 230>T_1>120(°C) 150>T_2>20(°C) However, T_1... Heat treatment temperature T_2... Stretching temperature
JP11695487A 1987-05-15 1987-05-15 Production of water-soluble crimped vinylon Pending JPS63282308A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11695487A JPS63282308A (en) 1987-05-15 1987-05-15 Production of water-soluble crimped vinylon

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11695487A JPS63282308A (en) 1987-05-15 1987-05-15 Production of water-soluble crimped vinylon

Publications (1)

Publication Number Publication Date
JPS63282308A true JPS63282308A (en) 1988-11-18

Family

ID=14699846

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11695487A Pending JPS63282308A (en) 1987-05-15 1987-05-15 Production of water-soluble crimped vinylon

Country Status (1)

Country Link
JP (1) JPS63282308A (en)

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