JPH0112848B2 - - Google Patents

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Publication number
JPH0112848B2
JPH0112848B2 JP58108943A JP10894383A JPH0112848B2 JP H0112848 B2 JPH0112848 B2 JP H0112848B2 JP 58108943 A JP58108943 A JP 58108943A JP 10894383 A JP10894383 A JP 10894383A JP H0112848 B2 JPH0112848 B2 JP H0112848B2
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JP
Japan
Prior art keywords
fibers
water
temperature
fiber
shrinkage
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
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JP58108943A
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Japanese (ja)
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JPS602709A (en
Inventor
Tsuneo Genma
Shunei Daito
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Kuraray Co Ltd
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Kuraray Co Ltd
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Priority to JP58108943A priority Critical patent/JPS602709A/en
Publication of JPS602709A publication Critical patent/JPS602709A/en
Publication of JPH0112848B2 publication Critical patent/JPH0112848B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は30〜40℃と言う比較的低温領域の温水
又は塩類を含む温水に対し短時間に大きな収縮率
と収縮力を示すことを特徴とする水膨潤高収縮性
繊維の製造方法に関するものである。 従来より水に浸漬すると吸水し膨潤或いは溶解
する繊維材料及びシート材料は知られている。例
えば、親水基をもつ樹脂より得られたポリビニル
アルコール系の水溶性繊維や繊維状で親水基を導
入した高吸水性繊維等が広く知られているが、こ
れ等は他素材に対し繊維状接着材として使用さ
れ、又他素材の加工性を保つのに用い、最終的に
溶解除去され、或いは吸水する事自体が目的とな
つている。従つてそれぞれの効果を発現する過程
で収縮することは目的遂行に対して阻害因子とな
る場合が多い。 更に疎水性樹脂を用いた熱収縮性繊維が知られ
ている。これ等の繊維はいずれも60℃以上比較的
高温領域でのみ収縮し、又冷却後は固化するので
本発明の低温高収縮性繊維の如くゴム状弾性を示
すことも不可能である。 本発明者は体温或いは風呂の温度程度の温水や
血液、尿等の塩類を含む温水に対し極めて敏感に
大きな収縮挙動を示す素材をうる可能性につき
種々検討を行つた結果、ある特殊条件で作られた
ポリビニルアルコール(以下PVAと略称する)
繊維が上記目的を達成し得ることを見出した。 即ち、親水性のPVA繊維を用い比較的低温領
域の温水中で繊維表面の部分溶解を起さず収縮発
現までの所要時間を短縮し、大きな収縮力を得る
ためには、吸水膨潤による繊維断面積の増大を図
るよりも、あらかじめ繊維内部の分子配向を不均
一状態で可能な限り進め、然も結晶化を必要最低
限に抑え、水と接触した瞬間における僅かな膨潤
作用で繊維内部に潜在する不均一な歪を緩和し、
この過程で発現する捲縮等の形態変化を利用する
方がより有効であると言う考え方が当該繊維材料
を発明するに当つて基本となつている。即ち本発
明は、重合度1200〜3000、鹸化度98.0モル%以上
のポリビニルアルコール水溶液を湿式紡糸し、得
られた紡糸糸篠を水分及び塩類を付着させた状態
で130℃以下の雰囲気中において4倍以上延伸し
たのち乾燥し、その後170℃以下の温度でかつ緊
張下で熱処理したのち、35℃以下の洗浄水を用い
て緊張下で水洗し、そして緊張下で繊維水分が50
%以下となるまで80℃以下で乾燥することを特徴
とする低温高収縮性繊維の製造法である。 PVAの繊維製造には乾式と湿式紡糸法がある
が湿式紡糸法を採用する。その理由は不織布用繊
維の製造に適している点もあるが、凝固に際し繊
維断面方向に不均一構造をとりやすいことがある
からである。 PVAの重合度は3000以上になると水溶液粘度
が著るしく上昇し生産性が大巾に低下するため好
ましくない。逆に1200以下では延伸時の分子配向
が劣り、所定の収縮力を得ることが困難となる。
また鹸化度を98モル%以下にすると、繊維に付着
した凝固液の塩類を水洗により除去するのに必要
な最低限の繊維中結晶化度が得られにくい。 PVA水溶液の湿式紡糸における凝固液として
は、通常硫酸ナトリウム、硫酸アンモニウム等の
塩の濃厚水溶液が用いられ、又水酸化ナトリウム
でゲル化後中和凝固する方式もあり、いずれでも
良いが、前者がより好ましい。 次に凝固浴を出たPVA繊維に対し膨潤水と凝
固液よりもたらした塩の水溶液が存在する状態で
130℃以下、経済的には100℃未満の雰囲気中にお
いて4倍以上延伸することで繊維内部に不均一な
歪を付与する。得られた繊維が比較的低温で吸水
時強い収縮挙動を示すためには、内部歪を可能な
限り不安定な状態で保持しなければならない。こ
の目的を達成するには繊維の結晶化を抑え分子配
向を極力大きくする条件が望ましい。分子配向を
増大するために高い延伸率が必要であり、この点
繊維温度の上昇が有効である。然し絶乾に近い状
態で繊維温度が150℃以上になると結晶化度が急
増し、結果的に内部歪は減少する。逆に繊維温度
が低いと延伸倍率が減少し必要な収縮力が得られ
なくなる。本発明者は、分子間隔を大きくとつて
結晶化を防ぎしかも大きな延伸倍率をとるため
に、PVAの溶媒である水を繊維内及び周囲に対
繊維40%以上含む状態で130℃以下の雰囲気中に
おいて4倍以上延伸することにより目的の収縮挙
動を得る可能性を見出した。延伸に際しては、付
着する硫酸ナトリウム、硫酸アンモニヤ等の凝固
能をもつ塩類は、繊維の過度の膨潤による実延伸
効率の低下を防ぐために、或いは部分溶解による
繊維間の膠着抑制のために十分な量を必要とす
る。なお延伸時における繊維自体の温度は多量の
水分を伴うので70℃以上100未満、好ましくは80
℃〜95℃の範囲に雰囲気温度を制御するのが望ま
しい。 延伸された繊維に付着している塩類は、精練工
程で0.5%以下まで水洗除去し、紡績或いは不織
工程に必要な油剤を付与した後乾燥して吸水時の
潜在収縮力をもちながら安定な形態の繊維を製造
する事が前提となるが、上記延伸後の繊維は、例
え緊張状態に置いても繊維表面の部分溶解なしに
塩類の水洗除去を行ない、乾燥した繊維を経済的
に生産することは困難である。従つて延伸された
繊維は塩類が付着した状態のまま絶乾し、必要最
低限の結晶化をほどこす目的で熱処理が必要とな
る。 熱処理条件を種々変化させ、繊維の収縮挙動を
調査した結果、極めて限られた条件において目的
とする吸水収縮性を示す繊維が得られることを確
認した。水中で繊維の収縮挙動を測定するには、
先ず繊維を直線状にするため繊維のデニール当た
り1/500(g)の初荷重をかけ、20℃の水中に入
れ、1℃/分で昇温させながら各温度における収
縮率を読みとる方法を採用した。繊維は水温の上
昇に伴つて収縮率を増大し最大収縮率を示す温度
で平衡となり、この温度を過ぎると荷重に抗しき
れず急激に伸長を始め切断する。切断する温度を
溶解温度と呼ぶことにする。 本発明の目的は体温近傍の水温において極めて
短時間に10%以上の収縮率を著るしいゴム弾性及
び適度の使用強度を示す繊維材料を提供すること
にある。したがつて少くとも50℃までは問題とな
るようなPVAの溶解が生じてはならない。この
領域は最高収縮温度65℃に対応する。然も前記延
伸条件を前提とした際この熱処理程度は繊維間の
接着なく経済的に付着塩類を定長下で水洗除去し
定長熱風乾燥しうる限界条件とたまたま一致す
る。次に熱処理効果を高めて行くと最大収縮率の
低下とその温度の上昇を伴うほか、繊維段階で必
要とする必要最小限の収縮率15%と最高収縮率を
示す両者の対応温度の差が縮少して来る。また本
発明の繊維を使用する紡績糸又は不織布が40℃の
水又は5%以下の塩を含む水の中で10%以上の急
激な収縮挙動を発現させるためには、それを構成
するPVA繊維が、繊維段階で水に浸漬したとき
約15%の収縮が必要となる。この物性を具備した
繊維の最高収縮温度は75℃となる。ただし、紡績
糸、不織布を製造する過程で室温の牽切切断方式
(パーロツク紡績等)を採用する場合、牽切時の
内部歪の増大を伴うので繊維の最高収縮温度は80
℃まで許容しうる。なお最大収縮率としては50%
以上が必要となり、最高収縮温度65℃より75℃、
(牽切切断方式では75℃を80℃と読みかえる。)と
言う三つの制限条件を満足する範囲内の熱処理条
件を選択しなければならない。このためには、後
述する実施例で行なわれているように170℃以下
の温度でかつ緊張下で熱処理する。 前述のように熱処理された当該PVA繊維に付
着している塩類は紡績或いは不織布化するため除
去し、水系エマルジヨン油剤処理を行う必要があ
る。水溶性の付着塩類を除去するためには水洗す
ることが最も経済的であるが水中膨潤で捲縮発現
の原動力である繊維内部歪を大きく減少さす事は
出来ない。本発明者は水洗の可能性につき種々検
討した結果、限定された条件下に湿潤状態でも強
い張力をかけると分子配向があまり乱れないこと
を利用し、洗滌水及び油剤処理液温度を35℃以下
に抑えると、熱処理工程と同様水洗、油剤処理、
対繊維水分が10%以下になるまでの乾燥は定長状
態以上の緊張下で処理可能なことを見出した。特
に塩類除去後の乾燥工程では対繊維水分が50%以
下となるまで熱風温度を80℃以下に抑えることが
繊維間の接着防止を図る上で有効である。 当該PVA繊維の単繊度に関しては上記物性を
満足する限り制約はない。然し通常生産される湿
式紡糸法の条件下では単繊度の増大に伴い凝固状
態が低下し、延伸効果が減少するため、好ましく
は7デニール(dr)以下の領域である。 次に当該PVA繊維からなる紡績糸及び不織布
について述べる。本発明方法により得られる低温
高収縮性繊維からなる紡績糸は尿又は血液に触れ
た際0.1g/dr以上の力で敏感に収縮することを前
提としており、40℃以下の水又は5%以下の塩を
含有する水の中で30秒以内に10〜60%収縮し湿潤
状態においてゴム状弾性を示す。測定法は30℃の
水、30℃の5%塩化ナトリウム水溶液及び人工尿
(尿素1.94℃、塩化ナトリウム0.80%、硫酸マグ
ネシウム7水塩0.11%、塩化カルシウム0.06%の
水溶液)の中と1/500(g/dr)の荷重をつけて
浸漬し収縮率の経時変化をそれぞれ読み取る。30
℃に比し40℃の場合収縮率はいずれも増大する。
紡績糸の製造は、捲縮を付与し紡績プロセスに適
合する長さに切断した上記繊維を用いカード方式
により紡出しても良いが、トウ状で牽切するパー
ロツク方式の方が繊維内部歪の増大、繊維長の上
昇による撚数減少での構成密度低下等の点で水中
における収縮率及び収縮力を向上するのに効果的
である。 なお他の繊維を混紡することもできる。40℃以
下の水又は5%以下の塩を含有する水に接触する
と30秒以内に10〜60%収縮する機能を具備した吸
水高収縮性不繊布は前記紡績糸と同様な効果を面
状で提供するものである。従つて捲縮を効率よく
発現さすためには実用性のある不織布の物性を示
す範囲内で繊維を一軸方向に可能な限り配列する
ことがより望ましいが限定するものではない。シ
ート状物質を得るためにはカード又はランダムウ
エバー後のウエブをニードルパンチで固定する
か、150℃未満の溶融温度をもち、然も溶融に際
し極めて僅かの収縮率しか示さないバインダー繊
維(例えば鐘紡製ベルトコンビ等の複合型バイン
ダー繊維)と混綿し熱接着させる等のプロセスを
採用するのが望ましい。吸水後の触感は必要によ
り10〜20%近傍のポリエステル等疎水性繊維を混
綿することで水中の収縮挙動、吸水時のゴム弾性
等目的とする物性を大きく損うことなく改良しう
る。 これ等の紡績糸或いは不織布は比較的低温領域
における湿潤高収縮性を利用し、例えば使い捨て
おむつに用いられているゴム状物質の代りに長手
方向端縁部に固定し、通常は大腿部を締付けるこ
となく、一旦尿が排出され当該紡績糸(紡績糸を
構成因子とする布状物を含む)或いは不織布が濡
れると迅速に収縮しおむつ外に洩れることを防ぐ
用途を始めとし、ギブスの補強布、その他水に濡
れると急速に収縮する性能を要求される分野に用
いることができる。 本発明方法により得られる低温高収縮性繊維は
また、乾燥させた状態で比較的柔軟でかつ水の存
在下においては、即座に吸水して100%以上の伸
びのあるゴム弾性を示す、極めて柔軟な性能を示
し、然も乾湿両状態でこれ等の性能は可逆性を有
するシート状或いは塊状物質に用いることもでき
る。 従来より吸水した場合柔軟なゴム状弾性を示す
素材としてホルマール化PVA樹脂の発泡スポン
ジ或いはPVA繊維を60℃以上の高温で収縮させ
た不織布が存在していた。然しこれ等の素材はい
ずれも乾燥状態で著るしく硬化するので用途が大
巾に限定され市場ではこの物性の改良要求が強
い。硬化する原因としてホルマール化PVA樹脂
スポンジの場合、可塑効果のある水が存在しなく
なると樹脂自体非常に硬い性質をもち、かつスポ
ンジ構造のため自由度がなく、じん性が大巾に低
下する。一方高温収縮PVA繊維よりなる不織布
では、先に述べた如く所定の収縮率を確保するに
必要な水温と最高収縮率に対応する水温或いは溶
解温度が接近するため、繊維表面において一部
PVAの溶解又は溶解に近い局部的な過大膨潤が
発生し乾燥すると硬化する。この硬化現象は繊維
間の擬似接着に基づくものであり、もみ加工をほ
どこすとある程度の柔軟化効果がみられるが、再
度吸水させた後は室温で乾燥してももみ加工前の
硬さに復元する。 本発明のPVA繊維よりなる不織布を30〜50℃
という比較的低温領域で面積を50℃以上収縮させ
ることにより得られた高密度不織布は、上記従来
品の欠点を改善しうる事を見出した。この高密度
不織布の表面は単繊度が細い程平滑となるが、カ
ードの通過性より0.5dr以上が必要である。不織
布の製造方式は乾式である限り何ら制約するもの
でなく、使用目的に適合したものを選択すれば良
い。収縮に方向性を与えないためには、ランダム
ウエバー或いは45゜のクロス方式を採用し、接着
にはニードルパンチ、150℃以下の融点をもち溶
融時収縮の小さい熱接着繊維の混綿状態における
熱処理等いずれの方式でも構わない。 不織布の目付、厚さもシート状から塊状原料ま
で用途により設定することができる。得られた不
織布は吸水時ゴム弾性を示し極めて柔軟な物性を
示し、かつ乾燥時においても柔軟性を保つが、採
用する条件によつては湿潤の際若干のぬめり感を
伴う場合がある。又湿潤時においても積極的にさ
らりとした感じを要求される用途もある。この対
策としてはポリエステル、ポリアクリルニトリル
或いはポリプロピレン等の通常生産されている疎
水性繊維或いは疎水性複合繊維を10〜20%あらか
じめ当該PVA繊維に混綿して置くと目的とする
物性を殆んど変えることなく改良可能である。又
目的により他の親水性繊維を混綿しても良い。然
し他繊維の混綿率が増加し70%を超えると不織布
において所望の収縮性が得られなくなる。 前述の如く本発明の当該PVA繊維よりなる不
織布を30〜50℃の比較的低い温水中で充分収縮さ
せた高密度不織布は吸水時直ちにゴム状弾性を示
し、極めてすぐれた柔軟性が得られかつ再び乾燥
しても柔軟性を殆んど失わない従来みられなかつ
た物性を示す。この物性を利用して顔面等に対す
る化粧の塗布或いはぬぐい落す用具類、湿布等の
基布、高級ワイパー、或いは海岸における埋立時
の洗掘防止用シート等の土木資材等に用いること
ができる。 以下本発明で得られる繊維および繊維構造物の
すぐれた性能を実施例により説明する。 実施例 1 重合度1700、ケン化度99.9モル%のPVA水溶
液を飽和Na2SO4水溶液中で湿式紡糸後40℃の空
気中及び90℃の飽和Na2SO4水溶液中で4.5倍に延
伸し、そのまま定長状態において絶乾するまで
130℃の熱風乾燥と、水中での最大収縮温度が70
℃になるよう170℃の熱風により熱処理を行つた。
この繊維は水による著るしい膨潤と収縮を伴うた
め定長を維持するに十分な張力を与えた状態で、
繊維付着Na2SO4除去を目的とする30℃の水洗、
給油等の湿潤処理を実施し、更に対繊維水分が40
%に到達するまで80℃次に120℃の熱風により緊
張下で乾燥した。得られた単繊度2drの繊維は繊
維間の接着が全くみられず良好な分繊性を示し、
水中における最大収縮率72%、溶解温度は79℃で
あつた。又30℃の蒸留水、人工尿及び食塩水中に
30秒浸漬したときの収縮率はそれぞれ31%、30%
及び16%と言う値を示した。 参考例 実施例1によつて得られた糸篠に捲縮を付与
し、繊維長51mmに切断したPVA繊維単独、及び
PVA繊維に単繊度2dr、繊維長51mmのポリエステ
ル繊維10%を混綿しランダムウエバー、ニードル
パンチ方式で目付80g/m2、針打数200p/cm2の乾
式不織布を作つた。当該不織布は蒸留水、人工尿
及び5%食塩水中で次表の如き収縮挙動が得られ
た。なお収縮後の湿潤状態において不織布は極め
てすぐれた柔軟性とゴム弾性を示し、更にPVA
繊維100%の場合にみられる表面のぬめり感は僅
かのポリエステル繊維を混綿することにより殆ん
ど消去することが出来た。
The present invention relates to a method for producing water-swellable highly shrinkable fibers that exhibit a large shrinkage rate and shrinkage force in a short period of time in hot water in a relatively low temperature range of 30 to 40°C or hot water containing salts. be. BACKGROUND OF THE INVENTION Fiber materials and sheet materials that absorb water and swell or dissolve when immersed in water are known. For example, polyvinyl alcohol-based water-soluble fibers obtained from resins with hydrophilic groups and superabsorbent fibers with hydrophilic groups introduced in fibrous form are widely known; It is used as a material, used to maintain the workability of other materials, and is ultimately dissolved and removed, or its purpose is to absorb water. Therefore, contraction during the process of expressing each effect often becomes an impediment to achieving the purpose. Furthermore, heat-shrinkable fibers using hydrophobic resins are known. All of these fibers shrink only at relatively high temperatures of 60° C. or higher, and solidify after cooling, so they are unable to exhibit rubber-like elasticity like the low-temperature, highly shrinkable fibers of the present invention. The present inventor conducted various studies on the possibility of producing a material that exhibits a large shrinkage behavior that is extremely sensitive to hot water at body temperature or bath temperature, or hot water containing salts such as blood and urine. polyvinyl alcohol (hereinafter abbreviated as PVA)
It has been found that fibers can achieve the above objectives. In other words, in order to use hydrophilic PVA fibers and shorten the time required for contraction to occur without causing partial dissolution of the fiber surface in hot water in a relatively low temperature range, and to obtain a large contractile force, fiber breakage due to water absorption and swelling is necessary. Rather than trying to increase the area, we try to advance the molecular orientation inside the fiber in a non-uniform state as much as possible in advance, while suppressing crystallization to the necessary minimum, and the slight swelling effect at the moment of contact with water creates the potential inside the fiber. Alleviates uneven distortion caused by
The idea that it is more effective to utilize morphological changes such as crimp that occur during this process is the basis for inventing the fiber material. That is, in the present invention, a polyvinyl alcohol aqueous solution having a degree of polymerization of 1,200 to 3,000 and a degree of saponification of 98.0 mol% or more is wet-spun, and the resulting spun yarn is spun in an atmosphere of 130°C or lower with moisture and salts attached. After stretching more than twice as much, it is dried, then heat treated at a temperature of 170°C or less and under tension, and then washed with washing water of 35°C or less under tension, and the fiber moisture is reduced to 50% under tension.
This is a method for producing low-temperature, highly shrinkable fibers, which is characterized by drying at 80°C or lower until the There are two methods for producing PVA fibers: dry spinning and wet spinning, but the wet spinning method is used. The reason for this is that although it is suitable for producing fibers for nonwoven fabrics, it tends to form a non-uniform structure in the fiber cross-sectional direction during coagulation. If the degree of polymerization of PVA exceeds 3000, the viscosity of the aqueous solution will increase significantly and the productivity will drop significantly, which is not preferable. On the other hand, if it is less than 1200, the molecular orientation during stretching will be poor and it will be difficult to obtain a predetermined shrinkage force.
Furthermore, if the degree of saponification is 98 mol% or less, it is difficult to obtain the minimum degree of crystallinity in the fibers necessary to remove salts of the coagulating liquid adhering to the fibers by washing with water. As a coagulating liquid in wet spinning of a PVA aqueous solution, a concentrated aqueous solution of salts such as sodium sulfate and ammonium sulfate is usually used, and there is also a method of gelling with sodium hydroxide and then neutralizing and coagulating. Either method is fine, but the former is more preferable. preferable. Next, the PVA fibers leaving the coagulation bath are treated with swelling water and an aqueous solution of salt brought from the coagulation solution.
Non-uniform strain is imparted to the inside of the fiber by stretching it four times or more in an atmosphere below 130°C, economically below 100°C. In order for the resulting fibers to exhibit strong shrinkage behavior upon water absorption at relatively low temperatures, the internal strain must be kept as unstable as possible. To achieve this objective, conditions are desirable that suppress crystallization of the fibers and maximize molecular orientation. A high stretching ratio is required to increase molecular orientation, and increasing the fiber temperature is effective in this regard. However, when the fiber temperature rises to 150°C or higher under conditions close to bone dry, the degree of crystallinity increases rapidly, resulting in a decrease in internal strain. Conversely, if the fiber temperature is low, the draw ratio decreases and the necessary shrinkage force cannot be obtained. In order to prevent crystallization by increasing the molecular spacing and to obtain a large stretching ratio, the present inventor developed a method in which water, which is a solvent for PVA, is contained in and around the fibers at a temperature of 130°C or less in a state where the fibers contain at least 40% of the fibers. We have discovered the possibility of obtaining the desired shrinkage behavior by stretching 4 times or more. During stretching, the adhering salts with coagulation ability, such as sodium sulfate and ammonium sulfate, should be used in an amount sufficient to prevent a decrease in actual stretching efficiency due to excessive swelling of the fibers, or to suppress adhesion between fibers due to partial dissolution. Requires. Note that the temperature of the fiber itself during stretching is 70°C or higher and lower than 100°C, preferably 80°C since it is accompanied by a large amount of moisture.
It is desirable to control the ambient temperature within a range of 95°C to 95°C. The salts adhering to the drawn fibers are washed away with water to less than 0.5% in the scouring process, and after applying the necessary oil for the spinning or non-woven process, they are dried to produce a stable material that retains latent shrinkage when water is absorbed. The prerequisite is to produce fibers in the form of fibers, but even if the fibers after stretching are placed under tension, salts can be washed away with water without any partial dissolution of the fiber surface, and dry fibers can be economically produced. That is difficult. Therefore, the drawn fibers are left to dry completely with the salts attached, and heat treatment is required to achieve the minimum necessary level of crystallization. As a result of investigating the shrinkage behavior of the fibers by varying the heat treatment conditions, it was confirmed that fibers exhibiting the desired water absorption and shrinkage properties could be obtained under extremely limited conditions. To measure the shrinkage behavior of fibers in water,
First, in order to make the fibers straight, an initial load of 1/500 (g) per denier of the fibers was applied, the fibers were placed in water at 20°C, and the shrinkage rate at each temperature was read while heating at 1°C/min. did. The shrinkage rate of the fibers increases as the water temperature rises, reaching an equilibrium at the temperature at which the fibers exhibit the maximum shrinkage rate, and beyond this temperature the fibers cannot resist the load and begin to elongate rapidly and break. The cutting temperature will be called the melting temperature. An object of the present invention is to provide a fiber material that exhibits remarkable rubber elasticity, shrinkage rate of 10% or more in an extremely short period of time at water temperatures close to body temperature, and moderate strength in use. Therefore, no problematic dissolution of PVA should occur up to at least 50°C. This region corresponds to a maximum shrinkage temperature of 65°C. However, assuming the above-mentioned stretching conditions, this degree of heat treatment coincides with the limit condition under which adhering salts can be economically removed by water washing over a fixed length and hot air drying over a fixed length without causing adhesion between fibers. Next, increasing the heat treatment effect will not only reduce the maximum shrinkage rate and increase its temperature, but also increase the difference in the corresponding temperature between the minimum shrinkage rate of 15% required at the fiber stage and the maximum shrinkage rate. It's shrinking. In addition, in order for the spun yarn or nonwoven fabric using the fibers of the present invention to exhibit a rapid shrinkage behavior of 10% or more in water at 40°C or water containing 5% or less salt, the PVA fibers constituting it must However, when immersed in water at the fiber stage, approximately 15% shrinkage is required. The maximum shrinkage temperature of fibers with this physical property is 75°C. However, if a room temperature stretch cutting method (such as parlock spinning) is used in the process of manufacturing spun yarn or nonwoven fabric, the maximum shrinkage temperature of the fiber is 80°C because internal strain increases during stretch cutting.
Tolerable up to ℃. The maximum shrinkage rate is 50%.
The above is required, and the maximum shrinkage temperature is 75℃ from 65℃.
(In the tension cutting method, 75°C can be read as 80°C.) Heat treatment conditions must be selected within a range that satisfies the following three limiting conditions. For this purpose, heat treatment is carried out at a temperature of 170° C. or lower and under tension, as carried out in the Examples described later. Salts adhering to the heat-treated PVA fibers as described above must be removed in order to be spun or made into a non-woven fabric, and treated with a water-based emulsion oil. Washing with water is the most economical way to remove water-soluble adhering salts, but swelling in water cannot greatly reduce the internal strain of fibers, which is the driving force behind crimp development. As a result of various studies on the possibility of washing with water, the present inventor took advantage of the fact that molecular orientation is not disturbed much when strong tension is applied even in a wet state under limited conditions, and set the temperature of the washing water and oil treatment solution to 35°C or less. As well as the heat treatment process, water washing, oil treatment,
It has been found that drying until the fiber moisture content is 10% or less can be carried out under tension greater than the constant length state. In particular, in the drying process after removing salts, it is effective to keep the hot air temperature below 80°C until the moisture content of the fibers is below 50% in order to prevent adhesion between the fibers. There are no restrictions on the single fineness of the PVA fiber as long as it satisfies the above physical properties. However, under the conditions of the wet spinning method that is normally used for production, the coagulation state decreases as the single fiber size increases, and the drawing effect decreases, so the range is preferably 7 denier (dr) or less. Next, the spun yarn and nonwoven fabric made of the PVA fiber will be described. It is assumed that the spun yarn made of low-temperature high shrinkage fibers obtained by the method of the present invention will sensitively contract with a force of 0.1 g/dr or more when it comes into contact with urine or blood, and that it will shrink sensitively with a force of 0.1 g/dr or more when it comes into contact with urine or blood. It shrinks by 10-60% within 30 seconds in water containing salt, and exhibits rubber-like elasticity in the wet state. The measurement method is water at 30℃, 5% sodium chloride aqueous solution at 30℃, and artificial urine (aqueous solution of urea 1.94℃, sodium chloride 0.80%, magnesium sulfate heptahydrate 0.11%, calcium chloride 0.06%) and 1/500. (g/dr) and read the change in shrinkage rate over time. 30
The shrinkage rate increases at 40℃ compared to ℃.
Spun yarn may be produced by a card method using the above-mentioned fibers, which are crimped and cut to a length suitable for the spinning process, but the parlock method, in which the fibers are cut in a tow shape, reduces the internal strain of the fibers. It is effective in improving the shrinkage rate and shrinkage force in water in terms of a decrease in structural density due to a decrease in the number of twists due to an increase in the fiber length and a decrease in the number of twists. Note that other fibers can also be blended. The water-absorbent highly shrinkable nonwoven fabric has the ability to shrink by 10 to 60% within 30 seconds when it comes into contact with water at 40°C or lower or water containing 5% or less salt, and has the same effect as the above-mentioned spun yarn in the form of a sheet. This is what we provide. Therefore, in order to efficiently develop crimp, it is more desirable to arrange the fibers in the uniaxial direction as much as possible within the range that exhibits the physical properties of a practical nonwoven fabric, but this is not limiting. To obtain a sheet-like material, the web after carding or random webs may be fixed with a needle punch, or binder fibers with a melting temperature of less than 150°C and showing very little shrinkage upon melting (for example, binder fibers manufactured by Kanebo Co., Ltd.) It is desirable to adopt a process such as blending with composite binder fibers such as Belt Combi and heat bonding. The feel after water absorption can be improved by blending around 10 to 20% hydrophobic fibers such as polyester, if necessary, without significantly impairing desired physical properties such as shrinkage behavior in water and rubber elasticity upon water absorption. These spun yarns or non-woven fabrics take advantage of their high wet shrinkage in relatively low temperature regions and are secured to the longitudinal edges, usually at the thighs, in place of the rubber-like materials used in disposable diapers, for example. Reinforcement of casts, including applications that prevent urine from leaking out of diapers, without tightening, once urine is drained, and when the spun yarn (including cloth-like materials whose constituent elements are spun yarn) or nonwoven fabric gets wet, it quickly shrinks and prevents urine from leaking outside the diaper. It can be used in fabrics and other fields that require the ability to rapidly shrink when wet. The low-temperature, high-shrinkage fiber obtained by the method of the present invention is also extremely flexible, being relatively flexible in a dry state and, in the presence of water, immediately absorbing water and exhibiting rubber elasticity with an elongation of more than 100%. It can also be used for sheet-like or bulk materials that exhibit excellent performance and are reversible in both wet and dry conditions. Conventionally, foamed sponges made of formalized PVA resin or nonwoven fabrics made by shrinking PVA fibers at high temperatures of 60°C or higher have existed as materials that exhibit flexible rubber-like elasticity when water is absorbed. However, since all of these materials harden significantly in the dry state, their uses are limited to wide ranges, and there is a strong demand in the market for improvements in their physical properties. In the case of formalized PVA resin sponges, the reason for hardening is that when water, which has a plasticizing effect, is no longer present, the resin itself is extremely hard, and the sponge structure has no flexibility, resulting in a significant decrease in toughness. On the other hand, in the case of nonwoven fabrics made of high-temperature shrink PVA fibers, as mentioned above, the water temperature required to ensure a predetermined shrinkage rate and the water temperature or melting temperature corresponding to the maximum shrinkage rate are close to each other, so some portions of the fiber surface may
PVA dissolves or localized excessive swelling similar to dissolution occurs, and when it dries, it hardens. This hardening phenomenon is based on pseudo-adhesion between fibers, and a certain degree of softening effect can be seen after kneading, but after reabsorbing water and drying at room temperature, the hardness remains the same as before kneading. Restore. The nonwoven fabric made of the PVA fiber of the present invention was heated at 30 to 50℃.
It has been discovered that a high-density nonwoven fabric obtained by shrinking the area by 50°C or more in a relatively low temperature region can improve the above-mentioned drawbacks of conventional products. The surface of this high-density nonwoven fabric becomes smoother as the fineness becomes finer, but 0.5 dr or more is required to ensure card passage. There are no restrictions on the manufacturing method of the nonwoven fabric as long as it is a dry method, and any method suitable for the purpose of use may be selected. In order to avoid directing the shrinkage, a random web or 45° cross method is used, needle punching is used for adhesion, and heat treatment is used in the blended state of heat-adhesive fibers that have a melting point of 150℃ or less and have low shrinkage when melted. Either method may be used. The basis weight and thickness of the nonwoven fabric can be set depending on the application, from sheet-like to bulk raw materials. The obtained nonwoven fabric exhibits rubber elasticity and extremely flexible physical properties when water is absorbed, and maintains flexibility even when dry, but depending on the conditions used, it may have a slightly slimy feel when wet. There are also applications where a smooth feel is required even when wet. As a countermeasure for this, mixing 10 to 20% of commonly produced hydrophobic fibers or hydrophobic composite fibers such as polyester, polyacrylonitrile, or polypropylene into the PVA fiber will almost change the desired physical properties. It can be improved without any problems. Further, other hydrophilic fibers may be mixed depending on the purpose. However, if the blending ratio of other fibers increases to more than 70%, the desired shrinkability cannot be obtained in the nonwoven fabric. As mentioned above, the high-density nonwoven fabric made by sufficiently shrinking the nonwoven fabric made of the PVA fiber of the present invention in relatively low-temperature water of 30 to 50°C exhibits rubber-like elasticity immediately upon absorption of water, and has extremely excellent flexibility. It exhibits unprecedented physical properties, with almost no loss of flexibility even after drying. Utilizing this physical property, it can be used for tools for applying or wiping off makeup on the face, etc., base fabrics such as poultices, high-grade wipers, and civil engineering materials such as sheets for preventing scouring during land reclamation on the coast. EXAMPLES The excellent performance of the fibers and fiber structures obtained by the present invention will be explained below using Examples. Example 1 A PVA aqueous solution with a polymerization degree of 1700 and a saponification degree of 99.9 mol% was wet-spun in a saturated Na 2 SO 4 aqueous solution and then stretched 4.5 times in air at 40°C and in a saturated Na 2 SO 4 aqueous solution at 90°C. , leave it at a constant length until completely dry.
Hot air drying at 130℃ and maximum shrinkage temperature in water is 70℃
Heat treatment was performed using hot air at 170°C to achieve a temperature of 170°C.
This fiber undergoes significant swelling and contraction due to water, so when sufficient tension is applied to maintain a constant length,
Washing with water at 30℃ for the purpose of removing Na 2 SO 4 attached to the fibers.
Performs moisture treatment such as oiling, and further reduces the fiber moisture content to 40%.
It was dried under tension with hot air at 80°C and then 120°C until reaching %. The obtained fibers with a single fineness of 2 dr showed no adhesion between fibers and exhibited good splitting properties.
The maximum shrinkage rate in water was 72%, and the dissolution temperature was 79°C. Also, in distilled water, artificial urine and saline at 30°C.
The shrinkage rate when immersed for 30 seconds is 31% and 30%, respectively.
and 16%. Reference example PVA fiber alone obtained by crimping the thread obtained in Example 1 and cutting it to a fiber length of 51 mm, and
A dry nonwoven fabric with a fabric weight of 80 g/m 2 and a needle count of 200 p/cm 2 was made by blending PVA fiber with 10% polyester fiber with a single fineness of 2 dr and a fiber length of 51 mm using a random web and needle punch method. The nonwoven fabric exhibited shrinkage behavior as shown in the following table in distilled water, artificial urine, and 5% saline. In addition, the nonwoven fabric exhibits extremely excellent flexibility and rubber elasticity in the wet state after shrinkage, and PVA
The slimy feeling on the surface that can be seen in the case of 100% fiber was almost completely eliminated by blending a small amount of polyester fiber.

【表】 向につき無荷重で測定した。
また実施例1により得られた糸篠に捲縮を付与
し、繊維長51mmに切断したPVA繊維単独及び
PVA繊維に単繊度2dr、繊維長51mmのポリエステ
ル繊維20%を混綿し、ランダムウエバー、ニード
ルパンチ方式で目付80g/m2、針打数200p/cm2
乾式不織布を作つた。更に当該不織布を40℃の水
中に1分間浸漬すると前者の不織布面積は浸漬前
の35%、後者の場合でも41%にまで収縮し、いず
れも極めてすぐれた柔軟性と200%近傍の湿潤切
断伸度をもつたゴム弾性を示す。特に後者では吸
水状態においてぬめりを感じさせない。収縮によ
り高密度化された不織布は80℃の熱風で乾燥した
あとも柔軟で、水中(水温40℃)への再浸漬と乾
燥を繰返した場合、再状態の触感は再現しうるこ
とを確認した。得られた高密度不織布の強伸度物
性を次表に示す。
[Table] Measurements were made with no load in the direction.
In addition, PVA fibers alone and PVA fibers obtained by crimping the yarn obtained in Example 1 and cutting them into fiber lengths of 51 mm and
A dry non-woven fabric with a fabric weight of 80 g/m 2 and a needle count of 200 p/cm 2 was made by mixing PVA fiber with 20% polyester fiber with a single fineness of 2 dr and a fiber length of 51 mm using a random web and needle punch method. Furthermore, when the nonwoven fabric was immersed in water at 40°C for 1 minute, the area of the nonwoven fabric shrunk by 35% of that before dipping, and by 41% in the latter case, showing extremely excellent flexibility and wet cutting elongation of nearly 200%. It exhibits a high degree of rubber elasticity. In particular, the latter does not feel slimy when water is absorbed. It was confirmed that the nonwoven fabric, which has been made highly densified by shrinkage, remains flexible even after being dried with hot air at 80°C, and that the tactile sensation in the re-conditioned state can be reproduced when it is repeatedly immersed in water (water temperature 40°C) and dried. . The strength and elongation properties of the obtained high-density nonwoven fabric are shown in the following table.

【表】 比較例 実施例1と同様の方式で湿式紡糸、延伸、乾燥
後、得られた繊維の最大収縮温度が85℃となるよ
う190℃の熱風中で熱処理を行い、定長で水洗、
給油、乾燥、捲縮及び切断処理をほどこした
PVA繊維単独の不織布を試作した。不織布の試
作条件は前記参考例に準ずる。 当該不織布の面積を水中で浸漬前の35%まで収
縮させるための水温は71℃が必要となり、得られ
た高密度不織布は吸水状態ですぐれた柔軟性とゴ
ム弾性を示す反面ぬめり感が非常に強く、特に乾
燥させた場合、たとえ80℃以下の熱風を用いても
非常に硬い板状を呈した。当該PVA繊維に20%
のポリエステル繊維を配合した高密度不織布では
ぬめり感を軽減しうるが乾燥後における硬さの改
善効果は殆んど認められない。 乾燥状態で板状を呈する不織布をもみ加工する
とある程度柔軟となるが、40℃以下の水に再浸漬
の上乾燥すると、その硬さはもみ加工前の水準ま
で復元した。
[Table] Comparative Example After wet spinning, stretching, and drying in the same manner as in Example 1, heat treatment was performed in hot air at 190°C so that the maximum shrinkage temperature of the obtained fiber was 85°C, and the fiber was washed with water at a fixed length.
Oiled, dried, crimped and cut
We prototyped a nonwoven fabric made of PVA fiber alone. The conditions for the trial production of the nonwoven fabric were as in the above reference example. In order to shrink the area of the nonwoven fabric in water to 35% of its pre-immersion water temperature, a water temperature of 71°C is required, and while the resulting high-density nonwoven fabric exhibits excellent flexibility and rubber elasticity in a water-absorbing state, it has a very slimy feel. It was strong, and especially when dried, it took on a very hard plate-like shape even when hot air of 80°C or less was used. 20% to the PVA fiber
A high-density nonwoven fabric containing polyester fibers can reduce the slimy feeling, but hardly any improvement in hardness after drying is observed. When the nonwoven fabric, which has a plate-like shape in the dry state, is kneaded, it becomes somewhat flexible, but when it is re-immersed in water below 40°C and dried, its hardness returned to the level before kneading.

Claims (1)

【特許請求の範囲】[Claims] 1 重合度1200〜3000、鹸化度98.0モル%以上の
ポリビニルアルコール水溶液を湿式紡糸し、得ら
れた紡糸糸篠を水分及び塩類を付着させた状態で
130℃以下の雰囲気中において4倍以上延伸した
のち乾燥し、その後170℃以下の温度でかつ緊張
下で熱処理したのち、35℃以下の洗浄水を用いて
緊張下で水洗し、そして緊張下で繊維水分が50%
以下となるまで80℃以下で乾燥することを特徴と
する低温高収縮性繊維の製造法。
1 Wet-spun a polyvinyl alcohol aqueous solution with a degree of polymerization of 1200 to 3000 and a degree of saponification of 98.0 mol% or more, and the resulting spun yarn with water and salts attached to it.
Stretched at least 4 times in an atmosphere of 130℃ or less, dried, then heat treated at a temperature of 170℃ or less under tension, washed with washing water at 35℃ or less under tension, and then dried under tension. Fiber moisture is 50%
A method for producing low-temperature, high-shrinkable fibers, which is characterized by drying at 80°C or lower until the following.
JP58108943A 1983-06-16 1983-06-16 Yarn having high shrinkage property at low temperature and its structure Granted JPS602709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58108943A JPS602709A (en) 1983-06-16 1983-06-16 Yarn having high shrinkage property at low temperature and its structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58108943A JPS602709A (en) 1983-06-16 1983-06-16 Yarn having high shrinkage property at low temperature and its structure

Publications (2)

Publication Number Publication Date
JPS602709A JPS602709A (en) 1985-01-09
JPH0112848B2 true JPH0112848B2 (en) 1989-03-02

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Country Link
JP (1) JPS602709A (en)

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JPH0718066B2 (en) * 1985-12-27 1995-03-01 株式会社クラレ Water absorption shrinkage yarn
JP2656245B2 (en) * 1985-11-01 1997-09-24 株式会社クラレ High speed shrink fiber and method for producing the same
JPH076086B2 (en) * 1986-06-05 1995-01-25 ユニチカ株式会社 Method for producing shrinkable polyvinyl alcohol-based filament
JP2588587B2 (en) * 1988-02-08 1997-03-05 株式会社クラレ Wet heat high shrinkage polyvinyl alcohol fiber
US5112903A (en) * 1989-07-04 1992-05-12 Sanyo Chemical Industries, Ltd. Articles molded from moisture shrinkable resins

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Publication number Priority date Publication date Assignee Title
JPS5188725A (en) * 1975-01-25 1976-08-03 HORIBINIRUARUKOORUKEIGOSEISENINOSEIZOHO
JPS521024A (en) * 1975-06-24 1977-01-06 Kaken Pharmaceut Co Ltd Germicides for agriculture and gardening
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Publication number Publication date
JPS602709A (en) 1985-01-09

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