JPS6260502B2 - - Google Patents
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- JPS6260502B2 JPS6260502B2 JP54130297A JP13029779A JPS6260502B2 JP S6260502 B2 JPS6260502 B2 JP S6260502B2 JP 54130297 A JP54130297 A JP 54130297A JP 13029779 A JP13029779 A JP 13029779A JP S6260502 B2 JPS6260502 B2 JP S6260502B2
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Description
本発明は、水膨潤性繊維の製造法に関するもの
であり、更に詳しくはアクリロニトリル系繊維
(以下AN系繊維という)に特定のアルカリを作用
させて該繊維外層部の少なくとも一部をヒドロゲ
ル化し、次いで特定の水混和性有機溶媒を付着、
乾燥することを要旨とする高水膨潤度かつ高物性
を有し、しかも膠着がなく柔軟な風合を有する水
膨潤性繊維の製造法に関するものである。
近年、高度の水膨潤性を有する重合体(ヒドロ
ゲル)が、その特殊機能に着目され幅広い用途分
野に適用されつつある。例えば、かかる重合体の
瞬間多量吸水能力を利用しておむつ、生理用品等
に、またその水分保持能力を利用して土壤改良
材、インスタント土のう等に、さらに人体組織と
の親和性に着目して軟質コンタクトレンズ、人工
臓器、外科用縫合材等に適用が試みられ、それら
の用途のうち既に実用化段階に入つたものもあ
る。
このように広範な適用可能性をもつヒドロゲル
は、その用途に応じて繊維形態にする方が好まし
い場合が少なくなく、かかる繊維状のヒドロゲル
もいくつか知られている。ところが、かかる既存
の天然もしくは合成の繊維においては、ある程度
の水膨潤性能をもつていてもその水膨潤度は極め
て低いものでしかなかつたり或は水溶性であつた
り、いずれにしても自重の数倍から数百倍の水を
吸収保持し、かつ水不溶性である水膨潤性繊維の
範畴からはほど遠いものでしかなかつた。また、
特公昭52―42916号公報において、アクリル系繊
維に特定の架橋構造と多量の塩の形のカルボキシ
ル基とを導入せしめてなる高膨潤性繊維状構造体
の記載がなされている。しかし、かかる繊維状構
造体には、極めて多量の塩型カルボキシル基が導
入されており、また繊維の内外層全体がヒドロゲ
ル化されているため高度の水膨潤性能を付与し得
る反面、非常に脆くまた膠着が著しく繊維の概念
からはほど遠いものでしかなかつた。また、特開
昭49―50217号公報において、鞘一芯型、海島
型、二成分貼り合せ型等の特殊紡糸法によつて加
水分解されやすいAN系重合体相の少なくとも一
部が繊維の外側に位置した複合繊維を出発物質と
して使用し、該AN系重合体相を架橋した後加水
分解して水膨潤性能を付与すると共に、加水分解
されにくい重合体相で繊維強力を維持させる技術
思想が開示されている。しかし、かかる発明にお
いては、特殊紡糸法により作製される高価な複合
繊維の使用を必須としており、しかも加水分解処
理に先立ち架橋処理を施す必要があり、工業的に
有利な方法とは言い難いものであつた。
ここにおいて本発明者は、上記の如き本質的欠
陥を克服し、何ら特殊な繊維を出発物質として使
用することなく、しかも別段の架橋処理工程を要
することなく繊維物性を保持しながら高度の水膨
潤性を有する繊維を得るべく鋭意検討した結果、
AN系繊維に、特定のアルカリ金属水酸化物水性
溶液を作用せしめて該繊維の外層部のみを選択的
にヒドロゲル化することにより、繊維物性を損う
ことなく水膨潤性能を有利に付与し得る事実を見
出し、先に特願昭53―46058号発明を提案した。
ところが、とりわけ繊維外層部を選択的にヒドロ
ゲル化した繊維、即ち繊維外層部に多量の塩型カ
ルボキシル基が導入された繊維は、後続の乾燥等
の工程において繊維同志が膠着し易く、かかる膠
着を回避し得る水膨潤性繊維の作製手段を提供す
ることが望まれていた。
このような状況下において、本発明者は、AN
系繊維に特定のアルカリを作用させて該繊維外層
部をヒドロゲル化し、特定の水混和性有機溶媒で
処理した後、乾燥することにより、高水膨潤度か
つ高物性を有し、しかも膠着がなく柔軟な風合の
水膨潤性繊維を製造し得る事実を見出し、本発明
に到達した。
即ち本発明の目的は、何ら特殊なAN系繊維を
出発物質として使用することなく優れた水膨潤性
能および繊維物性を兼備し、しかも膠着がなく柔
軟な風合を有する水膨潤性繊維の製造法を提供す
ることにある。
本発明の他の目的は、残留アルカリの除去、洗
浄、脱水、乾燥等の精製操作が容易な水膨潤性繊
維の製造法を提供することにあり、本発明の異な
る他の目的は、以下の明細書の記載により明らか
となろう。
上述した本発明の目的は、AN系繊維に
6.0mol/1000g溶液以上の高濃度アルカリ金属水
酸化物水性溶液または0.5mol/1000g溶液以上の
濃度の電解質塩類が共存する低濃度アルカリ金属
水酸化物水性溶液を100〜250℃の温度で30分間以
下作用させて0.1〜4.0mmol/gの塩型カルボキ
シル基(―COOX、Xはアルカリ金属または
NH4)を導入することにより該繊維外層部の少な
くとも一部がヒドロゲルからなり且つ残部がAN
系重合体及び/又は他の重合体からなる繊維を形
製し、得られた含水水膨潤性繊維を水混和時にお
ける水分率が液相より気相の方が大である水混和
性有機溶媒で処理した後、乾燥することにより、
工業的有利に達成することができる。
ここにおいて、本発明に係るAN系繊維とは、
AN系重合体の少なくとも一部が繊維表面に露出
した断面形状を有する繊維の総称であり、AN系
重合体単一成分紡糸繊維、二成分或は三成分以上
のAN系重合体の複合紡糸繊維、AN系重合体と他
の重合体、例えばポリ塩化ビニル系、ポリアミド
系、ポリオレフイン系、ポリスチレン系、ポリビ
ニルアルコール系、セルロース系等との複合紡糸
繊維等を挙げることができる。なお、各成分間の
剥離、水膨潤性能等の点でAN系重合体を単一成
分紡糸或は複合紡糸してなる繊維を出発アクリル
系繊維として採用することが好ましい。また、上
記AN系重合体とは、30重量%以上、好ましくは
50%以上のANを結合含有してなる重合体の総称
であり、AN単独重合体またはANと少なくとも1
種の他のエチレン系不飽和化合物との共重合体を
示称することは言うまでもなく、ANとでん粉、
ポリビニルアルコール等とのグラフト共重合体或
は前記AN単独重合体またはAN系共重合体と前記
他の重合体との混合重合体をも含むものである。
さらに、前記AN系重合体のAN含有率が本発明の
推奨範囲に満たない場合には、加水分解処理によ
つて充分な水膨潤性能を付与することができず好
ましくない。
なお、上記AN系繊維として潜在乃至顕在捲縮
を有する繊維を出発物質として使用することによ
り、捲縮を有し、腰、嵩高性等に優れた水膨潤性
繊維を作製することができ、好ましい。かかる
AN系繊維の捲縮特性としては、潜在乃至顕在捲
縮を有する限り何ら限定されるものではないが、
捲縮を顕在化させた状態において繊維長25mmあた
りの捲縮数(Cn)が3個以上、好ましくは5個
以上、捲縮度(Ci)が5%以上、好ましくは7
%以上であることが最終的に得られる水膨潤性繊
維製品の腰、嵩高性等の実用性能上望ましい。
かくして作製される繊維は短繊維、長繊維、繊
維トウ、糸、編織物、不織布等の形態により何ら
制約は認められず、またそれら繊維の乾燥物或は
含水物の如何を問わず本発明の出発物質として用
いることができ、またAN系繊維製造工程等にお
いて排出される廃繊維、或は該繊維製造工程中途
品(例えば、凝固糸、延伸糸、乾燥糸等)であつ
ても繊維形態を有する限り適用が可能である。
かかるAN系繊維を出発物質として高度の水膨
潤性及び高物性を有する水膨潤性繊維を得るため
には、AN系繊維の外層部のみを選択的にヒドロ
ゲル化して少なくとも繊維外層部の一部がヒドロ
ゲルからなる繊維となすことが必要である。かく
の如きAN系繊維の外層部のみを選択的にヒドロ
ゲル化し、しかも該外層部の割合を容易に制御し
得る一段加水分解、架橋処理方法として、本発明
においては以下に記載する手段を採用した。
即ち、前記乾燥状態或は含水状態のAN系繊維
に、6.0mol/1000g溶液以上の高濃度アルカリ金
属水酸化物水性溶液を作用させる(以下A法とい
う)か、または0.5mol/1000g溶液以上の濃度の
電解質塩を共存させた低濃度アルカリ金属水酸化
物水性溶液を作用させる(以下B法という)いず
れかの方法を採用した。尚、上記A法を採用する
に際し、6.0mol/1000g溶液未満の濃度のアルカ
リ水性溶液を作用させる場合には、AN系繊維は
加水分解反応により親水化されるものの水溶性と
なり、本発明の目的とするヒドロゲル外層部を形
成させることはできない。また、6.25〜
8.85mol/1000g溶液、更に6.25〜8.50mol/1000
g溶液の濃度範囲のアルカリ水性溶液を作用させ
ることにより、本発明をより効果的に達成するこ
とができる。かかる好適範囲の上限を越える条件
においては、アルカリ金属水酸化物の活動度が低
下するため反応速度を高めるためには高温処理が
必要となり、また残留アルカリの除去処理が困難
となるなど実用上好ましくない。また前記B法を
採用するに際し、共存させる塩が0.5mol/1000g
溶液未満の低濃度である場合には、AN系繊維は
加水分解反応により親水化されるもののその殆ん
どが水溶性となり、低濃度アルカリ水性溶液にて
一段の工程でヒドロゲル外層部を形成させること
はできない。また、1.0mol/1000g溶液以上の塩
濃度または該塩濃度及び0.5〜6.0mol/1000g溶
液、更に好ましくは1.0〜5.0mol/1000g溶液の
アルカリ金属水酸化物濃度のアルカリ水性溶液を
作用させることにより、本発明をより工業的有利
に実施することができる。
ここにおいて、本発明にて使用するアルカリ金
属水酸化物として、Na、K、Li等のアルカリ金
属類の水酸化物もしくはそれ等の混合物を挙げる
ことができ、また、電解質塩としては、アルカリ
処理条件下において安定である限りいかなる塩を
も採用することができ、該塩を構成する陽イオン
成分が例えば、Na、K、Li等のアルカリ金属
類;Be、Mg、Ca、Ba、等のアルカリ土類金属;
Cu、Zn、Al、Mn、Fe、Co、Ni等の他の金属
類;NH4等であり、また陰イオン成分が例えば塩
酸、硫酸、硝酸、炭酸、クロム酸、重クロム酸、
塩素酸、次亜塩素酸、有機カルボン酸、有機スル
ホン酸等の酸根等で構成される塩の1種もしくは
2種以上の混合物を挙げることができる。なお、
上記陽イオン成分が2価以上の元素である電解質
塩を用いる場合には、生成するヒドロゲル外層部
が凝集・合体し易く、また膨潤度が低下するた
め、アルカリ金属類を陽イオン成分とする塩を使
用する方が好ましい。なお、アルカリ水性溶液を
作製する溶媒としては、工業上水を使用すること
が好ましいが、水に代わる溶媒として、被処理
AN系繊維を溶解しない限り、メタノール、エタ
ノール、プロパノール、2―メトキシエタノー
ル、2―エトキシエタノール、ジメチルホルムア
ミド、ジメチルスルホキシド等の有機溶媒と水と
の混合溶媒を使用することができ、更に必要に応
じて他の無機系物質或は有機系物質を共存させる
ことも可能である。
ここにおいて、アルカリを作用させる具体的な
態様としては被処理AN系繊維を前記アルカリ水
性溶液中に浸漬したまま加熱する方法、或は前記
アルカリ水性溶液を付着させた後、加熱する方法
等を挙げることができるが、工業上、アルカリ水
性溶液を付着させた後、加熱する方法が好まし
い。かかる好適態様におけるアルカリ付着量とし
ては、繊維の乾燥重量に対して2〜200%、好ま
しくは5〜100%の範囲内に制御する必要があ
る。かかるアルカリ水性溶液の付着量が2%に満
たない場合には、本発明に推奨する特定のアルカ
リ水性溶液を作用させても所望の水膨潤度を有す
る繊維を作製することができず、またかかる付着
量が200%を越える場合には、水膨潤性能の向上
効果が頭打ちになるばかりか過剰のアルカリの除
去処理が困難となり、実用上好ましくない。
また、アルカリ水性溶液の所定量を繊維に付着
させる方法としては、該付着量を本発明の推奨範
囲内に制御し得る方法であれば何等制約は認めら
れず、例えば含水状態の被処理AN系繊維にアル
カリ金属水酸化物単独もしくはアルカリ金属水酸
化物と電解質塩との両者の粉末の所定量を付着さ
せたり、また乾燥状態もしくは含水状態の被処理
繊維にアルカリ水性溶液をスプレーし、所望によ
り遠心脱水機等で脱液したり、或は水性溶液中に
浸漬した後搾液、脱液する等の方法を挙げること
ができる。
なお、アルカリ水性溶液の付着量並びにアルカ
リ金属水酸化物或は電解質塩の濃度(付着量)を
容易に制御し得る点で、予め所定濃度に調製した
アルカリ水性溶液の所定量を乾燥状態の被処理
AN系繊維に付着させる態様が、工業上望まし
い。
上述した所定量のアルカリ水性溶液を付着させ
た繊維を次いで加熱し、加水分解処理を施す。
かかる加熱時の温度条件としては、一義的に規
定することは困難であるが、一般には高温下に作
用させる程反応速度は増大し処理効果を有利に達
成し得ることから80℃以上、好ましくは100〜250
℃の温度条件を採用することが望ましい。また、
加熱雰囲気として、飽和水蒸気、過熱水蒸気等の
湿熱雰囲気乃至加熱手段を採用するならば、温度
制御の容易さ、熱効率或は加水分解、架橋反応の
均質化等の点で好ましい。なお、熱ローラー、熱
板等の加熱手段を適宜使用することができること
は言うまでもない。
また、かかる加熱処理時間としては、被処理
AN系繊維の種類、アルカリ水性溶液の付着量、
加熱時の温度、或は目的とする水膨潤度等により
種々に変化させることが可能であり、一義的に規
定することは困難であるが、特に100〜250℃の加
熱温度条件を採用し、かつ好ましくは30分間以
下、更に好ましくは5秒〜20分間の範囲内におい
て加熱処理時間を調節することにより、本発明の
目的とする繊維外層部のみが選択的にヒドロゲル
化された水膨潤性繊維を工業的有利に作製するこ
とができる。
かくの如き本発明に推奨する特定の加水分解条
件を採用することにより、公知技術の条件下にア
ルカリ加水分解処理を施す場合には事実上水溶性
重合体のみを生成するにも拘らず、公知条件の反
応から予想される結果とは著しく異なり架橋処理
を施すことなく均質なヒドロゲルを、しかも高収
量にて生成する。かかる作用機構としては、とり
わけ繊維外層部におけるニトリル基の加水分解反
応に付随して、分子間の架橋結合もしくは分子内
の環状構造等の異種結合を形成する副反応等が、
前述の特定の条件において特異的に進行すること
等により説明し得るが、未だその詳細を解明する
に至つていない。
なお、かくして作製される水膨潤性繊維中に導
入する塩型カルボキシル基(―COOX)の量を
0.1〜4.0mmol/g、更に好ましくは0.5〜
3.5mmol/gの範囲内に調節することが望まし
い。該塩型カルボキシル基の量が本発明の推奨範
囲の下限を外れる場合には水膨潤性能が不充分と
なり、また該範囲の上限を越える場合には繊維物
性が低下すると共に柔軟性の乏しい脆いものしか
得られなくなり、望ましくない。
次に、このようにして作製された含水水膨潤性
繊維を水混和時における水分率が液相より気相の
方が大である水混和性有機溶媒で処理する必要が
ある。
ここにおいて、水混和時における水分率が液相
より気相の方が大である水混和性有機溶媒とは、
水混合系において水が優先的に蒸発する物理特性
を有する水混和性の有機溶媒を示称し、例えば次
のような溶媒を挙げることができる。
水と同程度かもしくは水より低い沸点を有
し、かつ水と極小沸点を与える共沸混合物(最
低共沸混合物)を形成し得る低沸点水混和性有
機溶媒、または該有機溶媒が極小沸点組成未満
の割合で水を含有する水性混合溶媒。
水より高い沸点を有し、かつ水と最低共沸混
合物を形成し得る高沸点水混和性有機溶媒、ま
たは該有機溶媒が極小沸点組成未満の割合で水
を含有する水性混合溶媒。
水より高い沸点を有し、かつ水と共沸混合物
を形成し得ない高沸点水混和性有機溶媒、また
は該有機溶媒が任意の割合で水を含有する水性
混合溶媒。
なお、上記第項に示される溶媒を使用するこ
とにより、とりわけ膠着が効果的に防止され柔軟
な風合を有する水膨潤性繊維を作製することがで
き、しかも後続の乾燥工程を工業的有利に実施す
ることができるので望ましい。かかる範畴に属す
る水混和性有機溶媒としては、エチルアルコー、
i―プロピルアルコール、n―プロピルアルコー
ル、sec―ブチルアルコール、t―ブチルアルコ
ール、アリルアルコール、アセトニトリル、アク
リロニトリル、酢酸エチル等を挙げることができ
る。また前記第項に属する溶媒としては、n―
ブチルアルコール、i―ブチルアルコール、n―
アミルアルコール、i―アミルアルコール、t―
アミルアルコール、シクロヘキサノール、n―ヘ
キシルアルコール、i―アミルエーテル等を挙げ
ることができる。なお、水を優先的に蒸発させ得
る限り、上記各項から選ばれた2種類以上の有機
溶媒を混用することもできる。
また、かかる溶媒処理は、アルカリ加水分解を
施した後そのままの、或は水洗、酸処理、所望の
塩型カルボキシル基への変換、脱水等の操作を適
宜施した含水(未乾燥状態の)水膨潤性繊維に施
す必要がある。なお、一旦乾燥した水膨潤性繊維
を溶媒で処理しても乾燥時に生起した膠着を消失
させることはできず、また粗硬な風合の繊維しか
得ることができないので、溶媒処理前の乾燥は避
けなければならない。また、本発明に係る特性を
満足しない溶媒を使用する場合には、後続の乾燥
工程において、水混和性有機溶媒が優先的に蒸発
して繊維に付着する水性混合溶媒中の水分率が漸
増し、やはり繊維間の膠着を回避することができ
ず、本発明の目的を達成することはできない。
而して、何ら特殊な繊維を出発物質として使用
しないでも少なくとも繊維外層部の一部がヒドロ
ゲルからなりAN系重合体及び/又は他の重合体
からなる内層部を有する繊維を得ることができ、
驚くべきことに該繊維は2〜300c.c./g、好まし
くは3〜200c.c./gの水膨潤度を有すると共に、
乾湿強度、乾湿伸度、結節強度等の繊維物性に関
しても通常の衣料用AN系繊維と殆ど遜色のない
水準の性能を発揮する。
本発明に係る上記溶媒処理を施すことにより、
繊維外層部が選択的にヒドロゲル化されているが
故に膠着を回避することは本質的に不可能である
と考えられていた水膨潤性繊維の膠着を効果的に
抑え、しかも柔軟な風合の繊維を提供し得た点が
本発明の特筆すべき利点である。
また、該繊維はAN系重合体等の内層部を有し
ている故、膨潤状態においても長さ方向の寸法変
化が起こらない特異な性質をも有している。
かくして、共重合成分として架橋形成単量体等
を含有する特殊な組成の重合体よりなる繊維或は
特殊紡糸法により作製される複合繊維等の使用を
要することなく、通常のAN系繊維もしくは該AN
系繊維等製造工程より排出される廃繊維、或は該
製造工程中途品等を出発物質として使用し、予め
架橋処理を施すことなくアルカリ水性溶液による
加水分解処理のみの工程によつて繊維外層部を選
択的にヒドロゲル化し得、また加水分解処理条件
の調節により、水膨潤度および物性の制御された
水膨潤性繊維を製造し得る点も、本発明の大きな
特徴である。また、かくして作製される水膨潤性
繊維は、膠着がなく、強度、伸度、腰、柔軟性等
均質かつ優れた物性を有しており、既存の衣料用
繊維等と全く同様の取扱いが可能である点も本発
明の特徴的利点である。
さらに、本発明に係る溶媒処理により、水膨潤
性繊維の洗浄、残留アルカリの除去等の精製操作
を兼ねることができ、また有機溶媒は水膨潤性繊
維を収縮させるため脱水効果をも有するので後続
の乾燥工程が容易になる点も本発明の効果として
挙げることができる。
かくの如き高度の水膨潤性及び優れた物性を兼
ね備えた本発明の水膨潤性繊維は、所望により単
独で、又は既存の天然、半合成もしくは合成繊維
等と混紡、混抄することにより、卓抜した吸湿
性、吸水性、保水性を有する新規な繊維素材或は
繊維製品としておむつ、生理用品、紙等に、或
は水と混和性のない有機溶剤からの脱水材、シー
ル材、カチオン交換繊維等に、更に既存のヒドロ
ゲル粉粒体と同様インスタント土のう、人工土
壤、水こけ、保温、保冷材等に適用することがで
きる。
本発明の理解を更に容易にするため、以下に実
施例を記載するが、本発明の要旨はこれ等実施例
の記載によつて何ら限定されるものではない。な
お、実施例に記載される百分率及び部は、特に断
りのない限り全て重量基準によるものである。
尚、以下の実施例に記載する水膨潤度、塩型カ
ルボキシル基(―COOX)量、嵩高性及び腰張り
性は下記の方法にて測定乃至算出したものであ
る。
(1) 水膨潤度(c.c./g)
試料繊維約0.1gを純水中に浸漬し25℃に保
ち24時間後、ナイロン布(200メツシユ)に
包み、遠心脱水機(30G×30分、但しGは重力
加速度)により繊維間の水を除去する。このよ
うにして調整した試料の重量を測定する(W1
g)。次に、該試料を80℃の真空乾燥機中で恒
量になるまで乾燥して重量を測定する(W2
g)。以上の測定結果から、次式によつて算出
した。従つて、本水膨潤度は、繊維の自重の何
倍の水を吸収保持するかを示す数値である。
水膨潤度=W1−W2/W2
(2) ―COOX基量(mmol/g)
十分乾燥した試料約1gを精〓し(Xg)、
これに200mlの水を加えた後、50℃に加温しな
がら1N塩酸水溶液を添加してPH2にし、次い
で0.1N苛性ソーダ水溶液で常法に従つて滴定
曲線を求めた。該滴定曲線からカルボキシル基
に消費された苛性ソーダ水溶液消費量(Yc.c.)
を求めた。以上の測定結果から、次式によつて
算出した。
―COOX基量=0.1Y/X
尚、多価カチオンが含まれる場合は、常法に
よりこれらのカチオンの量を求め、上式を補正
する必要がある。
(3) 嵩高性(m3/g)及び腰張り性(g/cm)
試料繊維約10gを開繊した後、10×10(cm)
の矩形に積み重ねて作成した試験片の重量を測
定する(W3g)。次に、該試験片を定速圧縮試
験機を用い100mm/分の速度で5g/cm2の圧縮
荷重まで圧縮―除重を3回繰返し、3回目の圧
縮曲線より0.5g/cm2初荷重時における試験片
の厚さ(hocm)を求め、次式によつて嵩高性
を算出した。
嵩高性=10×10×ho/W3
上記せる圧縮―除重を3回繰返した試験片
を、次いで50g/cm2の荷重まで圧縮を行なつて
求めた圧縮曲線から圧縮仕事量(腰張り性)を
試験片の厚さと圧縮荷重との積分値として算出
した。
実施例 1
90%のANおよび10%のアクリル酸メチルより
なるAN系繊維(単繊維繊度;3d、繊維長;51
mm、30℃のジメチルホルムアミド(DMF)溶液
中の固有粘度;1.3)5部を30%(7.5mol/1000
g溶液)苛性ソーダ水溶液95部中に浸漬し、撹拌
下に6分間煮沸し、次いで該繊維中の残留アルカ
リを水洗除去した後、i―プロピルアルコール中
に浸漬して水膨潤性繊維を収縮させると共に繊維
に付着する水を水分率が10%以下になるまでi―
プロピルアルコールで置換した後乾燥して白色乃
至微黄色を呈する水膨潤性繊維()を作製し
た。
このようにして得られた繊維()は水に溶解
せず、水膨潤状態でしごいてみたところAN系重
合体芯部が残つていることが、また1.8mmol/g
の―COONa基を含有し、103c.c./gの水膨潤度を
有することが確認された。また、該繊維()は
膠着が殆んどなく柔軟な風合を有していた。な
お、該繊維()の諸物性を測定した結果を、被
処理AN系繊維の物性値と共に第1表に記載す
る。
The present invention relates to a method for producing water-swellable fibers, and more specifically, acrylonitrile fibers (hereinafter referred to as AN fibers) are treated with a specific alkali to hydrogel at least a portion of the outer layer of the fibers, and then Attaching certain water-miscible organic solvents,
The present invention relates to a method for producing water-swellable fibers which have a high degree of water swelling and high physical properties by drying, and also have a soft texture without sticking. In recent years, highly water-swellable polymers (hydrogel) have attracted attention for their special functions and are being applied to a wide range of fields of use. For example, the ability of such polymers to instantly absorb a large amount of water can be used to make diapers, sanitary products, etc., the ability to retain moisture can be used to make soil improvers, instant sandbags, etc., and the polymer can also be made by focusing on its affinity with human tissue. Attempts have been made to apply it to soft contact lenses, artificial organs, surgical suture materials, etc., and some of these applications have already entered the stage of practical use. Hydrogels that have such wide applicability are often preferably in the form of fibers depending on their uses, and several such fibrous hydrogels are known. However, in existing natural or synthetic fibers, even if they have a certain degree of water swelling ability, their degree of water swelling is extremely low, or they are water soluble, and in any case, their own weight is very low. It is far from the category of water-swellable fibers, which absorb and retain from twice to several hundred times as much water and are insoluble in water. Also,
Japanese Patent Publication No. 52-42916 describes a highly swellable fibrous structure obtained by introducing a specific crosslinked structure and a large amount of carboxyl groups in the form of salt into acrylic fibers. However, such fibrous structures have extremely large amounts of salt-type carboxyl groups introduced into them, and the entire inner and outer layers of the fibers are hydrogel-formed, so while they can provide a high degree of water-swelling performance, they are extremely brittle. In addition, the stagnation was remarkable and the concept was far from the concept of fibers. Furthermore, in JP-A No. 49-50217, at least a part of the AN-based polymer phase that is easily hydrolyzed by special spinning methods such as single-core sheath type, sea-island type, and two-component bonding type is The technical idea is to use composite fibers located in the 200°C as a starting material, crosslink the AN polymer phase, and then hydrolyze it to impart water swelling properties, while maintaining fiber strength with a polymer phase that is difficult to hydrolyze. Disclosed. However, this invention requires the use of expensive composite fibers produced by a special spinning method, and also requires crosslinking treatment prior to hydrolysis treatment, making it difficult to say that it is an industrially advantageous method. It was hot. Here, the present inventor has overcome the above-mentioned essential defects and achieved high water swelling while maintaining fiber properties without using any special fibers as a starting material and without requiring a separate crosslinking process. As a result of intensive study to obtain fibers with
By applying a specific alkali metal hydroxide aqueous solution to AN-based fibers to selectively hydrogelize only the outer layer of the fibers, water swelling performance can be advantageously imparted without impairing the physical properties of the fibers. After discovering the facts, he first proposed the invention in patent application No. 46058/1983.
However, especially in fibers in which the outer layer of the fiber has been selectively hydrogelated, that is, in which a large amount of salt-type carboxyl groups have been introduced into the outer layer of the fiber, the fibers tend to stick together during the subsequent drying process. It was desired to provide a means of making water-swellable fibers that could avoid this. Under these circumstances, the inventor
By treating the outer layer of the fiber with a specific alkali to hydrogel it, treating it with a specific water-miscible organic solvent, and drying it, it has a high water swelling degree and high physical properties, and is non-sticky. The present invention was achieved by discovering the fact that water-swellable fibers with a soft texture can be produced. That is, the object of the present invention is to provide a method for producing water-swellable fibers that have excellent water-swelling performance and fiber properties without using any special AN-based fibers as a starting material, and have a flexible texture without sticking. Our goal is to provide the following. Another object of the present invention is to provide a method for producing water-swellable fibers that facilitates purification operations such as removal of residual alkali, washing, dehydration, and drying. This will become clear from the description of the specification. The purpose of the present invention described above is to
A high concentration alkali metal hydroxide aqueous solution with a concentration of 6.0mol/1000g or more or a low concentration alkali metal hydroxide aqueous solution coexisting with electrolyte salts with a concentration of 0.5mol/1000g or more at a temperature of 100 to 250℃ for 30 minutes. 0.1 to 4.0 mmol/g of salt-type carboxyl group (-COOX, X is an alkali metal or
By introducing NH 4 ), at least a part of the outer layer of the fiber is made of hydrogel and the rest is made of AN.
A water-miscible organic solvent in which the moisture content of the obtained water-containing water-swellable fiber is higher in the gas phase than in the liquid phase when mixed with water. By drying after processing with
This can be achieved with industrial advantage. Here, the AN-based fiber according to the present invention is
A general term for fibers with a cross-sectional shape in which at least a part of the AN polymer is exposed on the fiber surface, including AN polymer single component spun fibers, two-component or three or more component AN polymer composite spun fibers. , composite spun fibers of AN-based polymers and other polymers such as polyvinyl chloride-based, polyamide-based, polyolefin-based, polystyrene-based, polyvinyl alcohol-based, cellulose-based, and the like. In addition, from the viewpoint of release between each component, water swelling performance, etc., it is preferable to employ fibers formed by single-component spinning or composite spinning of AN-based polymers as the starting acrylic fibers. In addition, the above AN-based polymer is 30% by weight or more, preferably
It is a general term for polymers containing 50% or more of AN combined, and is an AN homopolymer or AN and at least 1
It goes without saying that the name refers to copolymers of AN and other ethylenically unsaturated compounds, such as AN and starch,
It also includes a graft copolymer with polyvinyl alcohol or the like, or a mixed polymer of the AN homopolymer or AN copolymer with the other polymer.
Furthermore, if the AN content of the AN-based polymer is less than the recommended range of the present invention, sufficient water swelling performance cannot be imparted by hydrolysis treatment, which is not preferable. In addition, by using fibers having latent or actual crimps as the above-mentioned AN-based fibers as starting materials, it is possible to produce water-swellable fibers having crimps and having excellent waist, bulkiness, etc., which is preferable. . It takes
The crimp characteristics of AN-based fibers are not limited in any way as long as they have latent or actual crimp.
The number of crimps (Cn) per 25 mm of fiber length is 3 or more, preferably 5 or more, and the crimp degree (Ci) is 5% or more, preferably 7 in a state where crimps are visible.
% or more is desirable from the viewpoint of practical performance such as stiffness and bulk of the water-swellable fiber product finally obtained. The fibers produced in this way are not restricted in any way by the form of short fibers, long fibers, fiber tows, threads, knitted fabrics, nonwoven fabrics, etc., and the present invention can be applied to the fibers regardless of whether they are dry or hydrated. It can be used as a starting material, and even waste fibers discharged from the AN fiber manufacturing process, etc., or products in the middle of the fiber manufacturing process (e.g., coagulated yarn, drawn yarn, dried yarn, etc.) can be used to change the fiber form. It can be applied as long as it has. In order to obtain water-swellable fibers having high water-swellability and high physical properties using such AN-based fibers as a starting material, only the outer layer of the AN-based fibers is selectively hydrogelated so that at least a part of the outer layer of the fibers is It is necessary to make fibers made of hydrogel. As a one-step hydrolysis and crosslinking treatment method that selectively hydrogelizes only the outer layer of such AN fibers and can easily control the ratio of the outer layer, the present invention employs the means described below. . That is, a highly concentrated alkali metal hydroxide aqueous solution of 6.0 mol/1000 g or more is applied to the dry or hydrated AN fiber (hereinafter referred to as method A), or a 0.5 mol/1000 g or more solution is applied One of the methods (hereinafter referred to as method B) in which a low concentration alkali metal hydroxide aqueous solution in the presence of a high concentration electrolyte salt was applied was employed. In addition, when employing the above method A, if an alkaline aqueous solution with a concentration of less than 6.0 mol/1000 g solution is applied, the AN fiber becomes hydrophilic due to the hydrolysis reaction, but becomes water-soluble, which does not meet the purpose of the present invention. It is not possible to form an outer hydrogel layer. Also, from 6.25
8.85mol/1000g solution, further 6.25-8.50mol/1000
The present invention can be more effectively achieved by using an alkaline aqueous solution in the concentration range of g solution. Under conditions exceeding the upper limit of this preferred range, the activity of the alkali metal hydroxide decreases, requiring high-temperature treatment to increase the reaction rate, and making it difficult to remove residual alkali, which is not practical. do not have. In addition, when adopting method B, the amount of salt to coexist is 0.5 mol/1000 g.
When the concentration is low, below that of the solution, the AN fiber becomes hydrophilic through a hydrolysis reaction, but most of it becomes water-soluble, and the outer layer of the hydrogel is formed in one step in a low-concentration alkaline aqueous solution. It is not possible. In addition, by acting with an aqueous alkali solution having a salt concentration of 1.0 mol/1000 g solution or more or an alkali metal hydroxide concentration of 0.5 to 6.0 mol/1000 g solution, more preferably 1.0 to 5.0 mol/1000 g solution. , the present invention can be implemented more industrially advantageously. Here, examples of the alkali metal hydroxide used in the present invention include hydroxides of alkali metals such as Na, K, and Li, or mixtures thereof, and examples of the electrolyte salt include alkali-treated Any salt can be used as long as it is stable under the conditions, and the cation component constituting the salt is, for example, alkali metals such as Na, K, Li, etc.; alkali metals such as Be, Mg, Ca, Ba, etc. earth metal;
Other metals such as Cu, Zn, Al, Mn, Fe, Co, Ni; NH4 , etc., and anionic components such as hydrochloric acid, sulfuric acid, nitric acid, carbonic acid, chromic acid, dichromic acid,
Examples include one type or a mixture of two or more types of salts composed of acid groups such as chloric acid, hypochlorous acid, organic carboxylic acids, and organic sulfonic acids. In addition,
When using an electrolyte salt whose cationic component is an element with a valence of 2 or higher, the outer layer of the hydrogel produced tends to aggregate and coalesce, and the degree of swelling decreases. It is preferable to use Although it is preferable to use industrial water as the solvent for preparing the alkaline aqueous solution, as a solvent in place of water,
As long as it does not dissolve the AN fibers, a mixed solvent of water and an organic solvent such as methanol, ethanol, propanol, 2-methoxyethanol, 2-ethoxyethanol, dimethylformamide, dimethyl sulfoxide, etc. can be used, and if necessary, It is also possible to coexist other inorganic or organic substances. Here, specific methods for applying the alkali include a method of heating the AN fiber to be treated while immersed in the aqueous alkaline solution, or a method of heating after adhering the aqueous alkaline solution. However, from an industrial perspective, it is preferable to apply the alkaline aqueous solution and then heat it. In such a preferred embodiment, the amount of alkali deposited needs to be controlled within the range of 2 to 200%, preferably 5 to 100%, based on the dry weight of the fiber. If the amount of the aqueous alkaline solution deposited is less than 2%, it will not be possible to produce fibers with the desired degree of water swelling even if the specific aqueous alkaline solution recommended in the present invention is applied. If the amount of adhesion exceeds 200%, not only will the effect of improving water swelling performance reach a plateau, but it will also become difficult to remove excess alkali, which is not preferred in practice. Furthermore, there are no restrictions on the method of attaching a predetermined amount of the alkaline aqueous solution to the fibers as long as the amount of the attached amount can be controlled within the recommended range of the present invention. A predetermined amount of powder of alkali metal hydroxide alone or both alkali metal hydroxide and an electrolyte salt is attached to the fiber, or an alkaline aqueous solution is sprayed onto the fiber to be treated in a dry or hydrated state, as desired. Examples of methods include removing the liquid using a centrifugal dehydrator or the like, or immersing it in an aqueous solution and then squeezing and removing the liquid. In addition, in order to easily control the amount of the aqueous alkaline solution deposited and the concentration (amount of deposited) of the alkali metal hydroxide or electrolyte salt, a predetermined amount of the alkaline aqueous solution prepared in advance at a predetermined concentration is applied to the dry surface. process
An embodiment in which it is attached to AN-based fibers is industrially desirable. The fibers coated with a predetermined amount of the aqueous alkaline solution described above are then heated and subjected to a hydrolysis treatment. Although it is difficult to define the temperature conditions during such heating, generally, the higher the temperature, the higher the reaction rate and the more advantageous the treatment effect can be achieved, so it is preferably 80°C or higher. 100~250
It is desirable to adopt temperature conditions of °C. Also,
It is preferable to use a moist heat atmosphere such as saturated steam or superheated steam or heating means as the heating atmosphere in terms of ease of temperature control, thermal efficiency, and homogenization of hydrolysis and crosslinking reactions. It goes without saying that heating means such as a hot roller or a hot plate can be used as appropriate. In addition, the heat treatment time is as follows:
Type of AN fiber, amount of alkaline aqueous solution attached,
It is possible to change it variously depending on the temperature during heating or the desired degree of water swelling, etc., and it is difficult to define it unambiguously, but in particular, a heating temperature condition of 100 to 250°C is adopted, By adjusting the heat treatment time preferably within 30 minutes, more preferably within the range of 5 seconds to 20 minutes, water-swellable fibers in which only the outer layer of the fibers is selectively hydrogelated, which is the object of the present invention. can be produced industrially advantageously. By employing the specific hydrolysis conditions recommended for the present invention, although the alkaline hydrolysis treatment under known conditions actually produces only water-soluble polymers, the known In contrast to the results expected from the reaction conditions, homogeneous hydrogels are produced without crosslinking, and in high yields. The mechanism of action is, in particular, side reactions that accompany the hydrolysis reaction of nitrile groups in the outer fiber layer, forming intermolecular crosslinks or heterogeneous bonds such as intramolecular cyclic structures.
This can be explained by the fact that it progresses specifically under the above-mentioned specific conditions, but the details have not yet been elucidated. In addition, the amount of salt type carboxyl group (-COOX) introduced into the water-swellable fiber thus prepared is
0.1~4.0mmol/g, more preferably 0.5~
It is desirable to adjust it within the range of 3.5 mmol/g. If the amount of the salt-type carboxyl group is outside the lower limit of the recommended range of the present invention, the water swelling performance will be insufficient, and if it exceeds the upper limit of the range, the physical properties of the fiber will deteriorate and the fiber will become brittle with poor flexibility. This is not desirable. Next, it is necessary to treat the hydrated water-swellable fiber thus produced with a water-miscible organic solvent whose moisture content when mixed with water is higher in the gas phase than in the liquid phase. Here, water-miscible organic solvents whose moisture content is higher in the gas phase than in the liquid phase when mixed with water are:
Refers to a water-miscible organic solvent that has the physical property that water preferentially evaporates in a water-mixed system, and includes, for example, the following solvents. A low-boiling water-miscible organic solvent that has a boiling point similar to or lower than that of water and that can form an azeotrope (lowest azeotrope) giving a minimum boiling point with water, or the organic solvent has a minimum boiling point composition. Aqueous mixed solvents containing water in proportions less than A high-boiling water-miscible organic solvent having a boiling point higher than water and capable of forming a minimum azeotrope with water, or an aqueous mixed solvent in which the organic solvent contains water in a proportion below the minimum boiling point composition. A high-boiling water-miscible organic solvent that has a boiling point higher than water and cannot form an azeotrope with water, or an aqueous mixed solvent in which the organic solvent contains water in any proportion. By using the solvents shown in the above item, it is possible to produce water-swellable fibers that effectively prevent sticking and have a soft texture, and also make the subsequent drying process industrially advantageous. This is desirable because it can be implemented. Water-miscible organic solvents that fall into this category include ethyl alcohol,
Examples include i-propyl alcohol, n-propyl alcohol, sec-butyl alcohol, t-butyl alcohol, allyl alcohol, acetonitrile, acrylonitrile, and ethyl acetate. In addition, as the solvent belonging to the above item, n-
Butyl alcohol, i-butyl alcohol, n-
amyl alcohol, i-amyl alcohol, t-
Examples include amyl alcohol, cyclohexanol, n-hexyl alcohol, and i-amyl ether. Note that two or more types of organic solvents selected from the above items may be used in combination as long as water can be evaporated preferentially. In addition, such solvent treatment may be carried out using aqueous (undried) water that has been subjected to alkaline hydrolysis and then used as is, or that has been subjected to appropriate operations such as washing with water, acid treatment, conversion to a desired salt-type carboxyl group, and dehydration. It is necessary to apply it to swellable fibers. Furthermore, even if the dried water-swellable fibers are treated with a solvent, it is not possible to eliminate the agglutination that occurs during drying, and only fibers with a rough texture can be obtained, so drying before solvent treatment is not recommended. Must be avoided. In addition, when using a solvent that does not satisfy the characteristics according to the present invention, the water-miscible organic solvent will preferentially evaporate in the subsequent drying process, and the water content in the aqueous mixed solvent that adheres to the fibers will gradually increase. However, sticking between the fibers cannot be avoided, and the object of the present invention cannot be achieved. Thus, even without using any special fiber as a starting material, it is possible to obtain a fiber in which at least a portion of the outer fiber layer is made of hydrogel and has an inner layer made of AN polymer and/or other polymers,
Surprisingly, the fibers have a water swelling degree of 2 to 300 c.c./g, preferably 3 to 200 c.c./g, and
In terms of fiber properties such as wet and dry strength, wet and dry elongation, and knot strength, it exhibits performance that is almost comparable to ordinary AN-based fibers for clothing. By performing the above solvent treatment according to the present invention,
It was thought that it was essentially impossible to avoid agglutination because the outer layer of the fibers was selectively hydrogelated, but it effectively suppresses agglutination of water-swellable fibers and has a flexible texture. It is a particular advantage of the present invention that fibers can be provided. Furthermore, since the fiber has an inner layer made of an AN-based polymer or the like, it also has the unique property of not undergoing dimensional change in the length direction even in a swollen state. In this way, it is not necessary to use fibers made of polymers with special compositions containing crosslinking monomers etc. as copolymerization components or composite fibers produced by special spinning methods. AN
Using waste fibers discharged from the production process of fibers, etc., or products in the middle of the production process, etc. as starting materials, the outer layer of the fibers is produced by a process of only hydrolysis treatment with an alkaline aqueous solution without prior crosslinking treatment. It is also a major feature of the present invention that water-swellable fibers with controlled water swelling degree and physical properties can be produced by selectively hydrogelating fibers, and by adjusting the hydrolysis treatment conditions. In addition, the water-swellable fibers produced in this way are non-adhesive and have homogeneous and excellent physical properties such as strength, elongation, elasticity, and flexibility, and can be handled in exactly the same way as existing clothing fibers. This is also a characteristic advantage of the present invention. Furthermore, the solvent treatment according to the present invention can serve as a purification operation such as washing the water-swellable fibers and removing residual alkali, and since the organic solvent also has a dehydration effect because it shrinks the water-swellable fibers, subsequent Another effect of the present invention is that the drying process becomes easier. The water-swellable fiber of the present invention, which has both such high water-swellability and excellent physical properties, can be used alone or by blending or making with existing natural, semi-synthetic or synthetic fibers, etc., as desired. New fiber materials or textile products with hygroscopicity, water absorption, and water retention properties, such as diapers, sanitary products, paper, etc., or dehydration materials from organic solvents that are immiscible with water, sealing materials, cation exchange fibers, etc. Furthermore, like existing hydrogel powders, it can be applied to instant sandbags, artificial soil, drainage, heat insulation, cold insulation materials, etc. In order to further facilitate understanding of the present invention, Examples are described below, but the gist of the present invention is not limited in any way by the description of these Examples. It should be noted that all percentages and parts described in the Examples are based on weight unless otherwise specified. In addition, the degree of water swelling, the amount of salt-type carboxyl group (-COOX), bulkiness, and waist tension described in the following examples were measured or calculated by the following method. (1) Degree of water swelling (cc/g) Approximately 0.1 g of sample fiber was immersed in pure water, kept at 25°C for 24 hours, then wrapped in nylon cloth (200 mesh) and placed in a centrifugal dehydrator (30G x 30 minutes). G is gravitational acceleration) to remove water between the fibers. Measure the weight of the sample prepared in this way (W 1
g). Next, the sample is dried in a vacuum dryer at 80°C until it reaches a constant weight, and the weight is measured (W 2
g). From the above measurement results, it was calculated using the following formula. Therefore, the actual water swelling degree is a numerical value indicating how many times the weight of the fiber can absorb and retain water. Degree of water swelling = W 1 - W 2 /W 2 (2) - COOX group amount (mmol/g) Approximately 1 g of a sufficiently dried sample was purified (Xg),
After adding 200 ml of water to this, a 1N aqueous hydrochloric acid solution was added while heating to 50°C to adjust the pH to 2, and then a titration curve was determined using a 0.1N aqueous sodium hydroxide solution according to a conventional method. From the titration curve, the amount of caustic soda aqueous solution consumed by carboxyl groups (Yc.c.)
I asked for From the above measurement results, it was calculated using the following formula. -COOX group amount = 0.1Y/X If polyvalent cations are included, it is necessary to determine the amount of these cations by a conventional method and correct the above formula. (3) Bulky property (m 3 /g) and waist tension property (g/cm) After opening approximately 10g of sample fiber, 10×10 (cm)
Measure the weight of the test pieces created by stacking them in a rectangular shape (W 3 g). Next, the test piece was compressed and unloaded three times using a constant speed compression tester at a speed of 100 mm/min to a compression load of 5 g/cm 2 , and from the third compression curve, the initial load was 0.5 g/cm 2 The thickness (hocm) of the test piece at the time was determined, and the bulkiness was calculated using the following formula. Bulkyness = 10 x 10 x ho/W 3. The compression work (waist tension property) was determined from the compression curve obtained by compressing the above-mentioned compression-unloading test piece three times and then compressing it to a load of 50 g/cm 2 . ) was calculated as the integral value of the thickness of the test piece and the compressive load. Example 1 AN-based fiber consisting of 90% AN and 10% methyl acrylate (single fiber fineness: 3 d , fiber length: 51
mm, intrinsic viscosity in dimethylformamide (DMF) solution at 30°C; 1.3) 5 parts to 30% (7.5 mol/1000
g solution) The fibers were immersed in 95 parts of aqueous caustic soda solution, boiled for 6 minutes while stirring, and then the residual alkali in the fibers was washed away, and then immersed in i-propyl alcohol to shrink the water-swellable fibers. Remove the water adhering to the fibers until the moisture content is below 10%.
After replacing with propyl alcohol, water-swellable fibers (2018) which were white to slightly yellow in color were produced by drying. The fibers obtained in this way did not dissolve in water, and when squeezed in a water-swollen state, it was found that the AN polymer core remained at 1.8 mmol/g.
It was confirmed that it contains a --COONa group of , and has a water swelling degree of 103 c.c./g. In addition, the fibers (2000) had almost no adhesion and had a soft texture. The results of measuring the physical properties of the fibers (2) are listed in Table 1 together with the physical property values of the AN fibers to be treated.
【表】
以上の結果より明らかなように、本発明に係る
水膨潤性繊維()は、膠着がなく柔軟な風合を
有し、強伸度、水膨潤度共に優れていることが理
解される。
一方、比較例として、10%および20%の苛性ソ
ーダ水溶液を使用する以外は上記処方に従つて加
水分解処理したところ、いずれの場合においても
被処理AN系繊維は水溶液中に溶解して粘稠な溶
液を形成したに留り、水膨潤性繊維に形成するこ
とはできなかつた。
また、煮沸時間を40分間に延長する外は上記処
方に従つて加水分解処理したところ、7.1mmol/
gの―COONa基を含有し、257c.c./gという極め
て大きな水膨潤度を有するものの、極めて脆く、
また該繊維を水膨潤状態でしごいてみたところ、
実質的にAN系重合体芯部は残存していなかつ
た。
また、溶媒処理を省略する以外は上記処方に従
つて水膨潤性繊維を作製したところ、膠着が著し
く、また風合も粗硬であつた。
実施例 2
実施例1記載のAN系繊維を開繊した後、該繊
維に4.0mol/1000g溶液の硝酸ソーダを共存させ
た2.5mol/1000g溶液の苛性ソーダ水溶液を均一
に撒布して30%付着させた。
次にこの繊維をオートクレーブ中に仕込み、
115℃の飽和水蒸気中で5分間加熱した後、実施
例1記載の処方に従つて溶媒処理、乾燥して水膨
潤性繊維()を作製した。
このようにして作製した繊維には膠着が殆んど
認められず柔軟な風合を有しており、また
1.3mmol/gの―COONa基を含有し、76c.c./g
の水膨潤度を有しており、さらにAN系重合体芯
部が残つており優れた強伸度特性を有することが
確認された。
また、i―プロピルアルコールの代りにt―ブ
チルアルコールを使用する以外は上記と同様にし
て処理したところ、やはり膠着が殆んど認められ
ず柔軟な風合を有する水膨潤性繊維()が得ら
れた。
実施例 3
二成分貼り合せ型AN系複合繊維(日本エクス
ラン工業(株)製、単繊維繊度;6d、繊維長;38
mm)を開繊した後、該繊維に30%苛性ソーダ水溶
液を均一に撒布して20%付着させた後、実施例2
記載の処方に従つて加熱、溶媒処理、乾燥して水
膨潤性繊維()を作製した。
この繊維()は1.5mmol/gのCOONa基を
含有し、AN系重合体芯部が残つており、また膠
着が殆んどなく柔軟な風合を有していた。なお、
この繊維()の諸性能を測定した結果を、被処
理AN系複合繊維の性能値と共に第2表に記載す
る。[Table] As is clear from the above results, it is understood that the water-swellable fibers () according to the present invention have a flexible texture without sticking, and are excellent in both strength and elongation and water-swellability. Ru. On the other hand, as a comparative example, hydrolysis treatment was carried out according to the above recipe except that 10% and 20% caustic soda aqueous solutions were used. In all cases, the treated AN fibers dissolved in the aqueous solution and became viscous. Only a solution was formed, and water-swellable fibers could not be formed. In addition, when the hydrolysis treatment was performed according to the above recipe except that the boiling time was extended to 40 minutes, 7.1 mmol/
Although it contains a -COONa group of 257 c.c./g and has an extremely high degree of water swelling of 257 c.c./g, it is extremely brittle.
In addition, when the fiber was squeezed in a water-swollen state,
Substantially no AN polymer core remained. Further, when water-swellable fibers were produced according to the above recipe except that the solvent treatment was omitted, the fibers showed significant adhesion and had a rough and hard texture. Example 2 After opening the AN-based fiber described in Example 1, a 2.5 mol/1000 g solution of caustic soda aqueous solution in which 4.0 mol/1000 g solution of sodium nitrate coexisted was uniformly spread on the fiber to give 30% adhesion. Ta. Next, this fiber is placed in an autoclave,
After heating in saturated steam at 115° C. for 5 minutes, the fibers were treated with a solvent according to the recipe described in Example 1 and dried to produce water-swellable fibers ( ). The fibers produced in this way have a soft texture with almost no adhesion, and
Contains 1.3 mmol/g of -COONa group, 76 c.c./g
It was confirmed that the material had a degree of water swelling of In addition, when treated in the same manner as above except that t-butyl alcohol was used instead of i-propyl alcohol, water-swellable fibers () with a soft texture and almost no adhesion were obtained. It was done. Example 3 Two-component bonded AN-based composite fiber (manufactured by Nippon Exlan Kogyo Co., Ltd., single fiber fineness: 6 d , fiber length: 38
Example 2
Water-swellable fibers ( ) were prepared by heating, solvent treatment, and drying according to the described recipe. This fiber () contained 1.5 mmol/g of COONa groups, had an AN polymer core remaining, and had a soft texture with almost no adhesion. In addition,
The results of measuring various performances of this fiber (2) are listed in Table 2 together with the performance values of the AN composite fiber to be treated.
【表】
数値、
以上の結果より明らかなように、本発明に係る
水膨潤性繊維()は、膠着、柔軟性、捲縮特
性、強伸度、嵩高性、腰張り性共に被処理AN系
複合繊維と殆んど遜色のない水準を維持してお
り、しかも卓抜した水膨潤性能が付与されている
ことが理解される。[Table] Numerical values,
As is clear from the above results, the water-swellable fiber according to the present invention has almost all the adhesion, flexibility, crimp properties, strength and elongation, bulkiness, and waist tension properties of the treated AN-based composite fiber. It is understood that it maintains a comparable level and has excellent water swelling performance.
Claims (1)
液以上の高濃度アルカリ金属水酸化物水性溶液ま
たは0.5mol/1000g溶液以上の濃度の電解質塩類
が共存する低濃度アルカリ金属水酸化物水性溶液
を100〜250℃の温度で30分間以下作用させて0.1
〜4.0mmol/gの塩型カルボキシル基(―
COOX、Xはアルカリ金属またはNH4)を導入す
ることにより該繊維外層部の少なくとも一部がヒ
ドロゲルからなり且つ残部がアクリロニトリル系
重合体及び/又は他の重合体からなる繊維を形製
し、得られた含水水膨潤性繊維を水混和時におけ
る水分率が液相より気相の方が大である水混和性
有機溶媒で処理した後、乾燥することを特徴とす
る水膨潤性繊維の製造法。 2 水膨潤性繊維が2c.c./g以上の水膨潤度を有
する繊維である特許請求の範囲第1項記載の製造
方法。[Scope of Claims] 1. High concentration alkali metal hydroxide aqueous solution of 6.0 mol/1000 g solution or more or low concentration alkali metal hydroxide aqueous solution in which electrolyte salts of 0.5 mol/1000 g solution or more coexist in acrylonitrile fiber. The solution is allowed to act at a temperature of 100-250℃ for no more than 30 minutes to reduce the concentration of 0.1
~4.0 mmol/g salt-type carboxyl group (-
By introducing COOX , A method for producing water-swellable fibers, which comprises treating the water-containing water-swellable fibers with a water-miscible organic solvent having a higher moisture content in the gas phase than in the liquid phase when mixed with water, and then drying the fibers. . 2. The manufacturing method according to claim 1, wherein the water-swellable fiber is a fiber having a degree of water swelling of 2 c.c./g or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13029779A JPS5658063A (en) | 1979-10-09 | 1979-10-09 | Production of water swellable fiber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP13029779A JPS5658063A (en) | 1979-10-09 | 1979-10-09 | Production of water swellable fiber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5658063A JPS5658063A (en) | 1981-05-20 |
| JPS6260502B2 true JPS6260502B2 (en) | 1987-12-16 |
Family
ID=15030940
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP13029779A Granted JPS5658063A (en) | 1979-10-09 | 1979-10-09 | Production of water swellable fiber |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5658063A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015224408A (en) * | 2014-05-29 | 2015-12-14 | 日本エクスラン工業株式会社 | Crosslinked acrylate fiber good in dispersibility |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6014028A (en) * | 1983-07-04 | 1985-01-24 | Matsushita Electric Ind Co Ltd | Filter for smoke and oil removal equipment |
| JPS61120795U (en) * | 1985-01-14 | 1986-07-30 | ||
| JP3971585B2 (en) * | 2001-05-07 | 2007-09-05 | ユニ・チャーム株式会社 | Body fluid absorbent sheet and body fluid absorbent article |
| DE102014219708A1 (en) * | 2014-09-29 | 2016-03-31 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Process for the thermal stabilization of fibers and fibers stabilized in this way |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5058311A (en) * | 1973-09-17 | 1975-05-21 | ||
| JPS5380493A (en) * | 1976-12-27 | 1978-07-15 | Japan Exlan Co Ltd | Preparation of hydrophilic crosslinked polymer |
-
1979
- 1979-10-09 JP JP13029779A patent/JPS5658063A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015224408A (en) * | 2014-05-29 | 2015-12-14 | 日本エクスラン工業株式会社 | Crosslinked acrylate fiber good in dispersibility |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5658063A (en) | 1981-05-20 |
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