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JP4041933B2 - Method for processing cellulosic fiber-containing woven or knitted fabric - Google Patents
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JP4041933B2 - Method for processing cellulosic fiber-containing woven or knitted fabric - Google Patents

Method for processing cellulosic fiber-containing woven or knitted fabric Download PDF

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Publication number
JP4041933B2
JP4041933B2 JP26742498A JP26742498A JP4041933B2 JP 4041933 B2 JP4041933 B2 JP 4041933B2 JP 26742498 A JP26742498 A JP 26742498A JP 26742498 A JP26742498 A JP 26742498A JP 4041933 B2 JP4041933 B2 JP 4041933B2
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Japan
Prior art keywords
resin
processing
dyeing machine
knitted fabric
hot water
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JP26742498A
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Japanese (ja)
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JPH11200248A (en
Inventor
雄一 柳内
正義 大場
一彦 市村
靖史 高木
一彦 原田
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Nisshinbo Holdings Inc
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Nisshinbo Holdings Inc
Nisshinbo Industries Inc
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Priority to JP26742498A priority Critical patent/JP4041933B2/en
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  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Chemical Or Physical Treatment Of Fibers (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、セルロース系繊維含有織編物を加工する方法に関し、更に詳述すると、セルロース系繊維含有織編物の防縮、防皺等の形態安定性を改善し、かつホルムアルデヒド系樹脂加工剤を用いた場合でも残留ホルムアルデヒドの少ないセルロース系繊維含有織編物の加工方法に関する。
【0002】
【従来の技術及び発明が解決しようとする課題】
従来より、セルロース系繊維織編物に防皺又は防縮性等の形態安定性能を付与するために、種々の樹脂加工剤や樹脂加工方法が検討されている。
【0003】
ところで、生地に皺がつくとか生地が縮む原因は、セルロースの非結晶領域の水素結合が外力又は水の作用によって壊され変形し、その状態で、再び水素結合が生成されることにより生じるものである。
【0004】
生地の樹脂加工による防皺又は防縮性の付与は、セルロース分子間に樹脂により架橋を生成させ、この架橋導入により上記水素結合が外力又は水の作用によって壊れにくくなることを利用したものであり、この場合、樹脂加工剤としては、グリオキザール系樹脂等の、いわゆる繊維素反応型樹脂を用いる方法が一般的である。
【0005】
しかしながら、従来の樹脂加工方法において、防皺又は防縮性を高める目的で樹脂付与量を増やした場合には、残留ホルムアルデヒドの増加がおこり、反対に樹脂付与量を減らした場合には、防皺又は防縮性が低下するといった相反する問題が生じ、実用上は防皺又は防縮性と残留ホルムアルデヒドの増加の相反する性質について、妥協できる範囲で樹脂加工を行っているのが現状である。
【0006】
また、例えば羽毛布団から羽毛が通過することを防止するための手段としては、羽毛布団用の綿織物を高圧カレンダー処理して綿織物の通気度を減らす方法が採用されている。しかし、綿織物は皺がつき易く、洗濯収縮が生じる。この場合、綿織物を液体アンモニア処理すると、皺も減り、防縮できるが、洗濯すると通気度が多くなり、羽毛通過のおそれが生じる。一方、樹脂を併用すると、通気度は洗濯後もある程度少なく保つことができるが、なお十分ではなく、手触りも硬い上、樹脂加工には上述したように通常ホルムアルデヒド系樹脂が使用されるので、残留ホルムアルデヒドの問題があり、羽毛布団のような残留ホルムアルデヒドの規制が厳しい用途では樹脂加工そのものが実施し難いという問題があった。
【0007】
本発明は上記事情を改善するためになされたもので、セルロース系繊維含有織編物に実用強度を保ちつつ防縮又は防皺性等の形態安定性を与え、しかも残留ホルムアルデヒドの問題もなく、手触りも良好であり、更に洗濯による特性変化の少ないセルロース系繊維含有織編物の加工方法を提供することを目的とする。
【0008】
【課題を解決するための手段及び発明の実施の形態】
本発明者は、上記目的を達成するため鋭意検討を行った結果、セルロース系繊維含有織編物を液体アンモニア処理した後、樹脂加工剤を付与し、次いで所定条件下で熱カレンダー処理又は該熱カレンダー処理及び所定温度で熱処理を施し、最後に所定温度で熱水処理することにより、上記織編物の形態安定性が改善され、単に樹脂加工を施した場合に比べて、この形態安定性が顕著に向上し、洗濯を繰り返しても初期の形態安定性が十分に維持されること、また樹脂加工剤としてホルムアルデヒド系樹脂を使用しても残留ホルムアルデヒドの問題がなく、手触りも良好であることを見出し、本発明をなすに至った。
【0009】
従って、本発明は、セルロース系繊維含有織編物を液体アンモニア処理した後、樹脂加工剤を付与し、次いで120〜200℃、ニップ圧200〜300kgf/cm、速度5〜15m/分で熱カレンダー処理又は該熱カレンダー処理及び120〜170℃で熱処理を施し、最後に98℃以上150℃未満で熱水に浸漬して処理することを特徴とするセルロース系繊維含有織編物の加工方法を提供する。この場合、用途によっては樹脂加工剤を付与した後、熱カレンダー処理を施し、次いで熱処理することが有効である。
【0010】
なお、本発明によると、防皺又は防縮に代表される形態安定性能が高くなり、かつ残留ホルムアルデヒドが極めて少なくなるのは、以下のような理由によるものと思われる。即ち、液体アンモニア処理により繊維が膨潤すると同時に結晶構造はセルロースI又はIIからセルロースIIIに転移をする。本発明では、繊維が膨潤した状態を保持したままで樹脂加工を施し、その後更に熱水処理するが、この処理により、樹脂加工で形成された形態を保持したままセルロースIIIからより安定な結晶構造であるセルロースI又はセルロースII結晶構造に戻すことができ、繊維が単に液体アンモニア処理のみ施した場合よりも更に安定な構造体となると共に、残留ホルムアルデヒドが除去されるものと考えられる。
【0011】
以下、本発明につき更に詳しく説明する。
本発明のセルロース系繊維含有織編物の加工方法は、セルロース系繊維含有織編物を下記の工程順序で処理するものである。
(1)液体アンモニア処理工程
(2)樹脂加工剤付与工程
(3)熱カレンダー処理工程
(4)熱処理工程
(5)熱水処理工程
この場合、(4)熱処理工程を必要により省略し得る。
【0012】
ここで、セルロース系繊維含有織編物を構成する繊維としては、綿、麻、レーヨン、ポリノジック、キュプラ、高強度再生セルロース繊維(例えば、商品名テンセル)等の天然繊維又は再生セルロース繊維が挙げられ、また、これら天然又は再生セルロース繊維にポリエステル、アクリル、ナイロン等の合成繊維を混用した複合繊維を用いることもできる。この場合、複合繊維中のセルロース系繊維の占める割合は一般に20重量%以上、特に40重量%以上であることが望ましい。これらのセルロース系繊維含有織編物には前処理として、必要に応じて毛焼、糊抜、精練、漂白、シルケット加工などの公知の処理を施すことができる。また該織編物は染色又はプリントされていてもよい。
【0013】
本発明の上記(1)工程は、液体アンモニア処理工程であり、これは常圧で−33℃以下の温度に保持された液体アンモニアに含浸する工程である。含浸方法としては、織編物を液体アンモニア浴中に浸漬する方法、織編物に液体アンモニアをスプレー又はコーティングする方法等が使用できる。含浸時間は適宜選定されるが、通常5〜40秒程度である。液体アンモニア処理後は、織編物に付着しているアンモニアを加熱により除去する。
【0014】
上記液体アンモニア処理後、(2)の樹脂加工剤の付与を行う。
この場合、樹脂加工剤は、セルロースの水酸基と反応し、架橋を生成するものであればいずれのものでもよく、このような化合物としては、例えばホルムアルデヒド、グリオキザール、グルタルアルデヒド等のアルデヒド類、ジグリシジルエーテルなどのエポキシ化合物、テトラブタンカルボン酸等のポリカルボン酸類、ジメチロール尿素、トリメチロールメラミン、ジメチロールエチレン尿素、ジメチロールジヒドロキシエチレン尿素などの繊維素反応型N−メチロール化合物が挙げられ、これらの中でも、特に繊維素反応型N−メチロール化合物が樹脂加工に伴う防皺又は防縮性能向上、生地強力低下とのバランスが良好である点から好ましい。
【0015】
上記樹脂加工剤の添加量は、樹脂加工を施すセルロース系繊維含有織編物の重量に対して、好ましくは固形分濃度で0.5〜10重量%、更に好ましくは1〜8重量%である。添加量が0.5重量%未満では樹脂加工としての効果が十分に発揮できない場合があり、8重量%を超えると樹脂加工に伴う強力低下が著しくなる場合がある。
【0016】
本発明の樹脂加工剤には、上記樹脂加工剤とセルロースの反応活性を高め、樹脂加工を迅速に行うために触媒を添加することができる。この触媒としては、通常樹脂加工に用いられる触媒であれば特に制限されず、例えば、ホウ弗化アンモニウム、ホウ弗化ナトリウム、ホウ弗化カリウム、ホウ弗化亜鉛等のホウ弗化化合物、塩化マグネシウム、硫酸マグネシウム、硝酸マグネシウム等の中性金属塩触媒、燐酸、塩酸、硫酸、亜硫酸、次亜硫酸、ホウ酸等の無機酸などが挙げられる。これら触媒には、必要に応じて助触媒としてクエン酸、酒石酸、林檎酸、マレイン酸等の有機酸などを併用することもできる。
【0017】
また、樹脂加工剤には、必要に応じて、セルロースと樹脂との反応を円滑に進めるための助剤を添加することができる。即ち、助剤は樹脂加工剤とセルロースの反応を促進させたり、架橋生成反応においても反応を均一に進めるといった反応溶媒としての作用、更にはセルロースを膨潤させる作用等を有するものである。
【0018】
上記助剤としては、例えば、グリセリン、エチレングリコール、ポリエチレングリコール、ポリプロピレングリコール等の多価アルコール類、エチレングリコールモノエチルエーテル、ジエチレングリコールモノエチルエーテル、エチレングリコールモノメチルエーテル、ジエチレングリコールモノメチルエーテル、ジエチレングリコールモノブチルエーテル等のエーテルアルコール類、ジメチルホルムアミド、モルホリン、2−ピロリドン、ジメチルアセトアミド、N−メチルピロリドン等の含窒素溶媒類、酢酸エチル、酢酸イソプロピル、酢酸ブチル、酢酸アミル、酢酸エチレングリコールモノメチルエーテル、酢酸エチレングリコールモノエチルエーテル、γ−ブチロラクトン等のエステル類などが挙げられる。
【0019】
なお、形態安定性として特に羽毛布団、ダウンジャケット等の通気度低下を目的とする場合、上記樹脂加工液に仕上剤(目詰剤)を添加することができる。仕上剤(目詰剤)としては、シリコーン・アクリル系樹脂、シリコーン・ポリウレタン系樹脂、アクリル系樹脂、ポリウレタン系樹脂、反応性シリコーンなど、公知のものを使用することができ、その添加量は、セルロース系繊維含有織編物の重量に対して、好ましくは固形分濃度で0.5〜3重量%、更に好ましくは1〜2重量%であり、所望する織編物の通気度に応じて適宜選定される。
【0020】
また、本発明の樹脂加工剤には、上述の薬剤の他に、必要に応じて、風合い調整用の柔軟剤や遊離ホルマリン濃度低減のためのホルマリンキャッチャー等を添加することもできる。
【0021】
本発明では、樹脂加工剤をセルロース系繊維含有織編物に付与するが、付与方法は特に制限されず、通常のパッドドライ法又は気相反応(VP反応)等の公知の方法を採用することができる。
【0022】
パッドドライ法は、樹脂加工剤を含む調合液に織編物を浸漬後、40〜120%の絞り率で絞り、雰囲気温度70〜100℃程度で水分を乾燥する。雰囲気温度が70℃未満では長い乾燥時間が必要となり、100℃を超えると樹脂加工剤のマイグレーションが起こり、加工剤が不均一に分布するなどの不都合を生じる場合がある。
【0023】
上記樹脂加工剤付与後、熱カレンダー処理を行う。特に通気度低下が求められる羽毛布団等では、これにより目つぶし効果がより有効に得られると同時に、樹脂反応が進行する。
【0024】
この熱カレンダー処理は常法によって行うことができ、通常120〜200℃、ニップ圧200〜300kg/cm、速度5〜15m/分とし、その条件は織編物の所望する通気度などによって選定することができる。
【0025】
次いで、熱処理を行い、樹脂反応を完結させる。ここで、熱カレンダー処理を上記のように行い、これによって上記樹脂反応を十分完結させることができる場合は、この熱処理を省略することができる。熱処理は、上記織編物を120〜170℃、好ましくは130〜160℃の温度で、1〜15分間、好ましくは2〜10分間熱処理し、架橋を生成させるもので、この熱処理の温度及び時間は添加する樹脂の種類、樹脂使用量、触媒の種類、触媒の添加量等に依存するが、熱処理温度が120℃未満では反応進行が遅くなり、170℃を超えると生地が黄変するなどの不都合を生じる場合がある。
【0026】
本発明においては、最後に熱水処理を行うもので、これにより上記(2)、並びに(3)及び/又は(4)の処理で達成された織編物の防皺及び防縮性に代表される形態安定性が顕著に向上し、洗濯しても形態安定性が効果的に保持されると共に、上記樹脂加工により生じるホルムアルデヒド残留の問題もなく、また手触りも良好な織編物が得られる。この場合、羽毛布団のように通気度低下性能が求められるものについてはこの性能が保持されるものである。
【0027】
ここで、熱水処理は、上記セルロース系繊維含有織編物を通常、98℃以上の温度の熱水で処理することにより行うことができる。具体的には、高圧で熱水処理ができる装置であればよく、例えば高圧液流染色機、高圧パドル染色機、高圧ドラム染色機、高圧ジッガー染色機、高圧ビーム染色機等を用いて処理することができ、生地品種や用途等に応じて、高圧液流染色機、高圧パドル染色機、高圧ドラム染色機等を用いて無緊張下で行うか、或いは高圧ジッガー染色機、高圧ビーム染色機等を用いて若干の緊張下で生地を平滑に保ったままで行うことができる。
【0028】
この場合、高圧液流染色機、高圧パドル染色機、高圧ドラム染色機等を用いて無緊張下で熱水処理する場合には、織編構造の応力が緩和され、防縮性が向上するといった利点がある上、熱水処理によるセット効果により湿防皺度が向上し、はり、こし感が付与されるとか、表面感に変化を付与させるなどの利点が生じるものである。
【0029】
また、高圧ビーム染色機、高圧ジッガー染色機を用いて若干の緊張下で熱水処理する場合には、熱水処理中に生地の平面性が保たれるために、生地に皺や凹凸が入らず、耳部が巻かず、更には、同時に大量の加工が可能となる等の利点がある。
【0030】
熱水処理の時間は適宜選定されるが、具体的には、熱水処理条件は下記の通りであることが好ましい。
(a)98℃以上105℃未満:2時間以上、好ましくは2.5時間以上
(b)105℃以上115℃未満:1時間以上、好ましくは1.5時間以上
(c)115℃以上125℃未満:40分以上、好ましくは1時間以上
(d)125℃以上135℃未満:30分以上、好ましくは1時間以上
(e)135℃以上150℃未満:20分以上、好ましくは1時間以上
なお、処理時間の上限は5時間であることが好ましい。
【0031】
上記熱水処理に際しては、熱水中に柔軟剤を添加して処理することができ、これにより、織編物に柔軟性を付与することができる。柔軟剤としては、高温で長時間処理した際に組成が変わらず、ソフトな風合いを付与するものであればよく、例えば脂肪酸アミド縮合化合物、脂肪酸エステル系化合物等の公知のものを使用し得、熱水中への添加量は0.1〜10重量%、特に0.3〜3重量%とすることができる。
【0032】
本発明の方法は、織編物の形態安定性が要望されるものに対して好適に採用される。この場合、最終加工織編物の通気度は所望によって選定されるが、羽毛布団、ダウンジャケット等に用いる織物にあっては、1cc以上3cc未満であることが好ましく、通気度が少なすぎると、発汗時の着用感が低下する場合がある。
【0033】
【発明の効果】
本発明によれば、防皺又は防縮に代表される形態安定性能が洗濯後においても保持され、残留ホルムアルデヒド等の問題もない優れたセルロース系繊維含有織編物が得られる。
【0034】
【実施例】
以下、実施例と比較例を示し、本発明を具体的に説明するが、本発明は下記の実施例に制限されるものではない。
【0035】
〔実施例1〕
綿160/2糸を使い、打ち込み本数,経231本/2.54cm,緯200本/2.54cmの経5枚朱子を常法に従って毛焼、糊抜、精練、漂白した後、−34℃で20秒間液体アンモニア処理し、次いで加熱により付着しているアンモニアを除去した。
【0036】
次に、表1に示す樹脂加工液を含浸し、マングルで余剰液を絞り出し、表1記載の付着量となるように調節した。続いて、乾燥後、160℃×200kg/cm×5m/分で熱カレンダー処理を行い、次いで160℃×2分間熱処理を行った。その後、巻取り方式で熱水処理(130℃×2時間)を行い、乾燥した。
【0037】
〔比較例1〕
実施例と同じ織物を毛焼、糊抜、精練、漂白、液体アンモニア処理した後、表1に示す仕上剤を含浸し、乾燥後、実施例と同条件で熱カレンダー処理を行った。
【0038】
以上の方法で得られた織物(羽毛布団用織物)の性能を評価し、表2に示す結果を得た。
【0039】
【表1】

Figure 0004041933
注:
1)リケンレジンLNB−20(三木理研工業社製)
2)カタリストM(大日本インキ化学工業社製)
3)シャリーヌEFE230(日信化学社製)
4)ソフボンP3000(竹本油脂社製)
5)ファインテックスNRW(大日本インキ化学工業社製)
【0040】
【表2】
Figure 0004041933
注:
6)JIS L1096 A法
7)JIS L1041 B法 アセチルアセトン法
8)JIS L1096 A法 ガーレ法
9)JIS L1096 D法 ペンジュラム法
10)JIS L1096 A法 ラベルドストリップ法
11)JIS L1059
【0041】
上記の結果より、実施例の方法が、洗濯後においても通気度が殆んど上がることがなく、初期の通気度にほぼ維持されること、また防皺度が高いにも拘らずホルマリン残留量が殆んどないこと、更に洗濯しても諸物性、防皺度、収縮率に大きな変動が生じることがないことが認められた。
【0042】
参考
40番双糸鹿の子(30インチ、18ゲージ)綿100%編物を常法でアルカリ処理及び漂白を施し、20秒間液体アンモニアで処理した後に、表3に示す樹脂処方・熱処理条件にて樹脂加工を行い、高圧液流加工機を用いて130℃×1時間熱水処理を行った後、脱水・乾燥し、テンターで柔軟剤加工を行い、所定の巾に仕上げた。
【0043】
参考
参考において、熱水処理の際に、熱水中に柔軟剤(AVIVAN SFC:脂肪酸アミド縮合化合物、チバガイギー社製)を5.0g/l添加したものを用いた以外は参考と同様に操作した。
【0044】
〔比較例2〕
表3に示す樹脂処方・熱処理条件にて樹脂加工を行った。この場合、この処方はホルマリン濃度を低く抑えたため、樹脂量を減じた処方となっている。
【0045】
以上の方法で得られた織物の性能を評価し、表3に示す結果を得た。
【0046】
【表3】
Figure 0004041933
注:
12)リケンレジンLNB−20:繊維素反応型N−メチロール樹脂(三木理研工業社製)
13)Cat.M:塩化マグネシウム系触媒(大日本インキ化学工業社製)
14)メイカテックスHP−780:可縫性向上剤(明成化学工業社製)
15)ソフミンSN−15:脂肪酸エステル系柔軟剤(ミヨシ油脂社製)
16)MSW−2:シリコン系柔軟剤(松本油脂製薬社製)
17)スミテックスバッファーFW:ホルマリンキャッチャー(住友化学社製)
18)PEG−200:ポリエチレングリコール(三洋化成工業社製)
19)AVIVAN SFC:脂肪酸アミド縮合化合物(チバガイギー社製)
【0047】
上記の結果の通り、参考例1は、比較例2に比べ、防縮性が良好であり、残留ホルムアルデヒドも少なく、更に実用強度も維持している。また、熱水処理時に浴中柔軟剤を添加した参考は、防縮性等の性能を損なわずに風合いがソフトになるものであった。[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for processing a cellulosic fiber-containing woven or knitted fabric. More specifically, the present invention improves the form stability of the cellulosic fiber-containing woven or knitted fabric, such as shrink-proofing and anti-molding, and uses a formaldehyde-based resin processing agent. Even in this case, the present invention relates to a method for processing a cellulosic fiber-containing woven or knitted fabric with little residual formaldehyde.
[0002]
[Prior art and problems to be solved by the invention]
Conventionally, various resin processing agents and resin processing methods have been studied in order to impart shape-stabilizing performance such as flaw prevention or shrinkage resistance to cellulosic fiber woven or knitted fabrics.
[0003]
By the way, the cause of wrinkles on the dough or shrinkage of the dough is caused by the fact that hydrogen bonds in the amorphous region of cellulose are broken and deformed by the action of external force or water, and in that state, hydrogen bonds are generated again. is there.
[0004]
The imparting of antifungal or shrinkage resistance by the resin processing of the dough is based on the fact that crosslinks are generated by the resin between cellulose molecules, and the hydrogen bonds are less likely to be broken by the action of external force or water due to the introduction of the crosslinks. In this case, as the resin processing agent, a method using a so-called fibrin-reactive resin such as glyoxal resin is generally used.
[0005]
However, in the conventional resin processing method, when the resin application amount is increased for the purpose of improving the anti-mold or shrinkage, the residual formaldehyde increases, and conversely, when the resin application amount is decreased, the anti-mold or There is a conflicting problem that the shrinkage resistance is lowered, and the present situation is that the resin processing is performed in a range that can be compromised with respect to the contradictory properties of the flaw prevention or shrinkage resistance and the increase in residual formaldehyde.
[0006]
For example, as a means for preventing the feather from passing through the duvet, a method of reducing the air permeability of the cotton fabric by applying a high-pressure calender treatment to the cotton fabric for the duvet. However, cotton fabrics are prone to wrinkling and cause laundry shrinkage. In this case, if the cotton fabric is treated with liquid ammonia, wrinkles are reduced and shrinkage can be prevented. However, if the cotton fabric is washed, the air permeability increases and the possibility of passing through the feathers arises. On the other hand, when the resin is used in combination, the air permeability can be kept to some extent after washing, but it is still not sufficient and the touch is hard, and the resin processing usually uses a formaldehyde-based resin as described above. There is a problem of formaldehyde, and there is a problem that it is difficult to carry out resin processing itself in applications where the regulation of residual formaldehyde is severe, such as duvets.
[0007]
The present invention has been made in order to improve the above-described circumstances, and gives the cellulosic fiber-containing woven or knitted fabric with form stability such as shrink-proofing or anti-molding while maintaining practical strength, and there is no problem of residual formaldehyde and the touch is also good. An object of the present invention is to provide a method for processing a cellulosic fiber-containing woven or knitted fabric that is good and has little property change due to washing.
[0008]
Means for Solving the Problem and Embodiment of the Invention
The present inventor has conducted extensive investigations to achieve the above objects, after the cellulosic fiber-containing textile fabric with liquid ammonia treatment, and imparting resin finishing agent and then heat calendering or the heat calender under a predetermined condition processing and subjected to Netsusho management at a predetermined temperature, by treatment with hot water and finally with a predetermined temperature, the form stability of the woven or knitted fabric are improved, simply compared with the case of applying the resin processing, the shape stability is Remarkably improved, the initial form stability is sufficiently maintained even after repeated washing, and there is no problem of residual formaldehyde even when formaldehyde resin is used as a resin processing agent, and the touch is also good. The headline and the present invention were made.
[0009]
Accordingly, in the present invention, after the cellulose fiber-containing woven or knitted fabric is treated with liquid ammonia, a resin processing agent is applied, and then a thermal calendar treatment is performed at 120 to 200 ° C., a nip pressure of 200 to 300 kgf / cm, and a speed of 5 to 15 m / min. or subjected to Netsusho management in the heat calendering treatment and 120 to 170 ° C., provides a method of processing cellulosic fiber-containing textile fabric which comprises treating by immersion in hot water is less than the last 98 ° C. or higher 0.99 ° C. To do. In this case, depending on the application, it is effective to apply a heat calendering treatment after applying a resin processing agent, and then heat-treat.
[0010]
In addition, according to the present invention, the reason why the form stability performance represented by antifouling or shrinkage is high and the residual formaldehyde is extremely low is considered to be as follows. That is, the fiber is swollen by the liquid ammonia treatment, and at the same time, the crystal structure is transferred from cellulose I or II to cellulose III. In the present invention, the resin is processed while maintaining the state where the fibers are swollen, and then further subjected to hot water treatment. By this treatment, a more stable crystal structure from cellulose III while maintaining the form formed by the resin processing It is considered that the cellulose I or cellulose II crystal structure can be returned to, and the structure becomes more stable than the case where the fiber is only subjected to the liquid ammonia treatment, and the residual formaldehyde is removed.
[0011]
Hereinafter, the present invention will be described in more detail.
The processing method of the cellulosic fiber-containing woven or knitted fabric of the present invention is a treatment of the cellulosic fiber-containing woven or knitted fabric in the following process sequence.
(1) Liquid ammonia treatment step (2) resin finish applying process (3) the heat calendering step (4) the heat treatment step (5) the hot-water treatment step in this case, may be omitted if necessary to about (4) Heat treatment Engineering.
[0012]
Here, the fibers constituting the cellulose-based fiber-containing woven or knitted fabric include natural fibers such as cotton, hemp, rayon, polynosic, cupra, high-strength regenerated cellulose fibers (for example, trade name Tencel) or regenerated cellulose fibers, In addition, composite fibers obtained by mixing these natural or regenerated cellulose fibers with synthetic fibers such as polyester, acrylic, and nylon can also be used. In this case, the proportion of the cellulosic fibers in the composite fiber is generally 20% by weight or more, and particularly preferably 40% by weight or more. These cellulosic fiber-containing woven or knitted fabrics can be subjected to known treatments such as hair firing, desizing, scouring, bleaching, mercerizing, etc., as pretreatment, as necessary. The woven or knitted fabric may be dyed or printed.
[0013]
The step (1) of the present invention is a liquid ammonia treatment step, which is a step of impregnating liquid ammonia maintained at a temperature of −33 ° C. or lower at normal pressure. As the impregnation method, a method of dipping a woven or knitted fabric in a liquid ammonia bath, a method of spraying or coating liquid ammonia on a woven or knitted fabric, or the like can be used. The impregnation time is appropriately selected and is usually about 5 to 40 seconds. After the liquid ammonia treatment, the ammonia adhering to the woven or knitted fabric is removed by heating.
[0014]
After the liquid ammonia treatment, the resin processing agent (2) is applied.
In this case, the resin processing agent may be any resin as long as it reacts with the hydroxyl group of cellulose to form a crosslink. Examples of such compounds include aldehydes such as formaldehyde, glyoxal, and glutaraldehyde, and diglycidyl. Examples include epoxy compounds such as ethers, polycarboxylic acids such as tetrabutanecarboxylic acid, fibrin-reactive N-methylol compounds such as dimethylol urea, trimethylol melamine, dimethylol ethylene urea, and dimethylol dihydroxy ethylene urea. Among these, In particular, a fibrin-reactive N-methylol compound is preferred from the viewpoint of good balance between improvement in anti-mold or anti-shrinkage performance associated with resin processing and reduction in fabric strength.
[0015]
The addition amount of the resin processing agent is preferably 0.5 to 10% by weight, more preferably 1 to 8% by weight, based on the weight of the cellulosic fiber-containing woven or knitted fabric subjected to resin processing. If the addition amount is less than 0.5% by weight, the effect as the resin processing may not be sufficiently exhibited, and if it exceeds 8% by weight, the strength reduction accompanying the resin processing may be remarkably increased.
[0016]
A catalyst can be added to the resin processing agent of the present invention in order to increase the reaction activity of the resin processing agent and cellulose and to perform resin processing quickly. The catalyst is not particularly limited as long as it is a catalyst usually used for resin processing, and examples thereof include borofluoride compounds such as ammonium borofluoride, sodium borofluoride, potassium borofluoride, zinc borofluoride, and magnesium chloride. And neutral metal salt catalysts such as magnesium sulfate and magnesium nitrate, and inorganic acids such as phosphoric acid, hydrochloric acid, sulfuric acid, sulfurous acid, hyposulfite and boric acid. These catalysts can be used together with an organic acid such as citric acid, tartaric acid, apple acid, maleic acid, etc. as a co-catalyst, if necessary.
[0017]
Moreover, the auxiliary | assistant for advancing reaction of a cellulose and resin smoothly can be added to a resin processing agent as needed. That is, the auxiliary agent has an action as a reaction solvent that promotes the reaction between the resin processing agent and cellulose, or promotes the reaction even in the cross-linking reaction, and further has an action of swelling the cellulose.
[0018]
Examples of the auxiliary agent include polyhydric alcohols such as glycerin, ethylene glycol, polyethylene glycol, and polypropylene glycol, ethylene glycol monoethyl ether, diethylene glycol monoethyl ether, ethylene glycol monomethyl ether, diethylene glycol monomethyl ether, and diethylene glycol monobutyl ether. Nitrogen-containing solvents such as ether alcohols, dimethylformamide, morpholine, 2-pyrrolidone, dimethylacetamide, N-methylpyrrolidone, ethyl acetate, isopropyl acetate, butyl acetate, amyl acetate, ethylene glycol monomethyl ether, ethylene glycol monoethyl acetate Examples include esters such as ether and γ-butyrolactone.
[0019]
In addition, a finish agent (clogging agent) can be added to the resin processing liquid when the purpose of form stability is to reduce the air permeability of duvets, down jackets and the like. As finishing agents (clogging agents), known ones such as silicone / acrylic resins, silicone / polyurethane resins, acrylic resins, polyurethane resins, reactive silicones, and the like can be used. The solid content concentration is preferably 0.5 to 3% by weight, more preferably 1 to 2% by weight, based on the weight of the cellulosic fiber-containing woven or knitted fabric, and is appropriately selected according to the desired air permeability of the woven or knitted fabric. The
[0020]
In addition to the above-mentioned chemicals, a softening agent for adjusting the texture, a formalin catcher for reducing free formalin concentration, and the like can be added to the resin processing agent of the present invention as necessary.
[0021]
In the present invention, the resin processing agent is applied to the cellulosic fiber-containing woven or knitted fabric, but the application method is not particularly limited, and a known method such as a normal pad dry method or a gas phase reaction (VP reaction) may be employed. it can.
[0022]
In the pad dry method, a woven or knitted fabric is dipped in a preparation liquid containing a resin processing agent, then squeezed at a drawing rate of 40 to 120%, and moisture is dried at an ambient temperature of about 70 to 100 ° C. If the atmospheric temperature is less than 70 ° C., a long drying time is required, and if it exceeds 100 ° C., migration of the resin processing agent occurs, which may cause inconveniences such as uneven distribution of the processing agent.
[0023]
After the resin processing agent is applied , a thermal calendar process is performed. In particular, in a duvet or the like for which a decrease in air permeability is required, the crushing effect can be obtained more effectively, and at the same time, the resin reaction proceeds.
[0024]
This thermal calendering process can be carried out by a conventional method, usually 120 to 200 ° C., nip pressure 200 to 300 kg / cm, speed 5 to 15 m / min, and the conditions are selected according to the desired air permeability of the woven or knitted fabric. Can do.
[0025]
Next, heat treatment is performed to complete the resin reaction. Here, when the heat calendar process is performed as described above and the resin reaction can be sufficiently completed, the heat treatment can be omitted. The heat treatment is performed by heat-treating the woven or knitted fabric at a temperature of 120 to 170 ° C., preferably 130 to 160 ° C. for 1 to 15 minutes, preferably 2 to 10 minutes to form a crosslink. Depending on the type of resin to be added, the amount of resin used, the type of catalyst, the amount of catalyst added, etc., the reaction progresses slowly when the heat treatment temperature is less than 120 ° C, and the fabric becomes yellow when it exceeds 170 ° C. May occur.
[0026]
In the present invention, the hot water treatment is performed at the end, and this is represented by the anti-warming and shrink-proof properties of the woven or knitted fabric achieved in the above-mentioned treatments (2) and (3) and / or (4). The morphological stability is remarkably improved, and the woven or knitted fabric having a good form feeling and no problem of residual formaldehyde caused by the resin processing can be obtained while the morphological stability is effectively maintained even after washing. In this case, this performance is maintained for a material that requires a low air permeability such as a duvet.
[0027]
Here, the hot water treatment can be performed by treating the cellulose fiber-containing woven or knitted fabric with hot water having a temperature of 98 ° C. or higher. Specifically, any apparatus capable of performing hydrothermal treatment at high pressure may be used. For example, processing is performed using a high-pressure liquid dyeing machine, a high-pressure paddle dyeing machine, a high-pressure drum dyeing machine, a high-pressure jigger dyeing machine, a high-pressure beam dyeing machine, or the like. Depending on the fabric type and application, it can be done under no tension using a high pressure liquid dyeing machine, a high pressure paddle dyeing machine, a high pressure drum dyeing machine, etc., or a high pressure jigger dyeing machine, a high pressure beam dyeing machine, etc. Can be used while keeping the fabric smooth under slight tension.
[0028]
In this case, when hydrothermal treatment is performed without tension using a high-pressure liquid dyeing machine, a high-pressure paddle dyeing machine, a high-pressure drum dyeing machine, etc., the stress of the woven / knitted structure is relieved and the shrinkage resistance is improved. In addition, the moisture-proofing degree is improved by the setting effect by the hot water treatment, and there are advantages such as imparting a beam, a squeaky feeling, and imparting a change to the surface feeling.
[0029]
In addition, when hot water treatment is performed under slight tension using a high-pressure beam dyeing machine or high-pressure jigger dyeing machine, the flatness of the dough is maintained during the hot water treatment, so that wrinkles and irregularities may enter the dough. In addition, there is an advantage that the ear portion is not wound and that a large amount of processing can be performed at the same time.
[0030]
The hot water treatment time is appropriately selected, but specifically, the hot water treatment conditions are preferably as follows.
(A) 98 ° C. or more and less than 105 ° C .: 2 hours or more, preferably 2.5 hours or more (b) 105 ° C. or more and less than 115 ° C .: 1 hour or more, preferably 1.5 hours or more (c) 115 ° C. or more and 125 ° C. Less than: 40 minutes or more, preferably 1 hour or more (d) 125 ° C. or more and less than 135 ° C .: 30 minutes or more, preferably 1 hour or more (e) 135 ° C. or more and less than 150 ° C .: 20 minutes or more, preferably 1 hour or more The upper limit of the treatment time is preferably 5 hours.
[0031]
In the hot water treatment, a softening agent can be added to the hot water for treatment, thereby imparting flexibility to the woven or knitted fabric. As the softening agent, the composition does not change when treated at a high temperature for a long time, as long as it imparts a soft texture, for example, known ones such as fatty acid amide condensation compounds and fatty acid ester compounds can be used, The amount added to the hot water can be 0.1 to 10% by weight, particularly 0.3 to 3% by weight.
[0032]
The method of the present invention is suitably used for those in which shape stability of a woven or knitted fabric is desired. In this case, the air permeability of the final processed woven or knitted fabric is selected as desired. However, in the woven fabric used for the duvet, down jacket, etc., it is preferably 1 cc or more and less than 3 cc. Sometimes wearing feeling may be reduced.
[0033]
【The invention's effect】
According to the present invention, an excellent cellulosic fiber-containing woven or knitted fabric is obtained that retains its form-stable performance typified by anti-molding or shrink-proofing even after washing and has no problems such as residual formaldehyde.
[0034]
【Example】
EXAMPLES Hereinafter, although an Example and a comparative example are shown and this invention is demonstrated concretely, this invention is not restrict | limited to the following Example.
[0035]
[Example 1]
Using cotton 160/2 yarn, hair sacrificing, desizing, scouring, and bleaching according to a conventional method for warp 5 pieces of warp, 231 warp / 2.54 cm, weft 200 / 2.54 cm, −34 ° C. Was treated with liquid ammonia for 20 seconds, and then the attached ammonia was removed by heating.
[0036]
Next, the resin processing liquid shown in Table 1 was impregnated, excess liquid was squeezed out with a mangle, and it adjusted so that it might become the adhesion amount of Table 1. Subsequently, after drying, a heat calendar treatment was performed at 160 ° C. × 200 kg / cm × 5 m / min, and then a heat treatment was performed at 160 ° C. × 2 minutes. Then, the hot water process (130 degreeC * 2 hours) was performed by the winding system, and it dried.
[0037]
[Comparative Example 1]
The same fabric as in the example was subjected to hair burning, desizing, scouring, bleaching, and liquid ammonia treatment, impregnated with a finishing agent shown in Table 1, dried, and then subjected to thermal calendering treatment under the same conditions as in the example.
[0038]
The performance of the woven fabric obtained by the above method (woven fabric for duvet) was evaluated, and the results shown in Table 2 were obtained.
[0039]
[Table 1]
Figure 0004041933
note:
1) Riken Resin LNB-20 (Miki Riken Kogyo Co., Ltd.)
2) Catalyst M (Dainippon Ink Chemical Co., Ltd.)
3) Charine EFE230 (manufactured by Nissin Chemical)
4) Softbon P3000 (Takemoto Yushi Co., Ltd.)
5) Finetex NRW (Dainippon Ink Chemical Co., Ltd.)
[0040]
[Table 2]
Figure 0004041933
note:
6) JIS L1096 Method A 7) JIS L1041 Method B Acetylacetone Method 8) JIS L1096 Method A Gurley Method 9) JIS L1096 Method D Pendulum Method 10) JIS L1096 Method A Labeled Strip Method 11) JIS L1059
[0041]
From the above results, the method of the example shows that, even after washing, the air permeability is hardly increased, the initial air permeability is substantially maintained, and the formalin residual amount is high despite the high degree of fouling. It was confirmed that there was almost no change in the physical properties, the degree of weathering, and the shrinkage rate even after washing.
[0042]
[ Reference Example 1 ]
No. 40 twin yarn Kanoko (30 inch, 18 gauge) 100% cotton knitted fabric is subjected to alkali treatment and bleaching in the usual way, treated with liquid ammonia for 20 seconds, and then processed with resin formulation and heat treatment conditions shown in Table 3 After performing a hydrothermal treatment at 130 ° C. for 1 hour using a high-pressure liquid flow processing machine, it was dehydrated and dried, processed with a softener using a tenter, and finished to a predetermined width.
[0043]
[ Reference Example 2 ]
In Reference Example 1 , similar to Reference Example 1 except that a softener (AVIVAN SFC: fatty acid amide condensation compound, manufactured by Ciba Geigy) was added to hot water during the hot water treatment. Operated.
[0044]
[Comparative Example 2]
Resin processing was performed under the resin prescription and heat treatment conditions shown in Table 3. In this case, this formulation is a formulation with a reduced amount of resin because the formalin concentration is kept low.
[0045]
The performance of the fabric obtained by the above method was evaluated, and the results shown in Table 3 were obtained.
[0046]
[Table 3]
Figure 0004041933
note:
12) Riken Resin LNB-20: Fibrin-reactive N-methylol resin (Miki Riken Kogyo Co., Ltd.)
13) Cat. M: Magnesium chloride catalyst (Dainippon Ink Chemical Co., Ltd.)
14) Maycatex HP-780: Sewing improver (manufactured by Meisei Chemical Co., Ltd.)
15) Sofmin SN-15: fatty acid ester softener (manufactured by Miyoshi Yushi Co., Ltd.)
16) MSW-2: Silicone softener (Matsumoto Yushi Seiyaku Co., Ltd.)
17) Sumitex buffer FW: formalin catcher (manufactured by Sumitomo Chemical Co., Ltd.)
18) PEG-200: Polyethylene glycol (manufactured by Sanyo Chemical Industries)
19) AVIVAN SFC: fatty acid amide condensation compound (Ciba Geigy)
[0047]
As shown in the above results, Reference Examples 1 and 2 have better shrinkage resistance than Comparative Example 2, have less residual formaldehyde, and maintain practical strength. Further, in Reference Example 2 in which the softening agent in the bath was added during the hot water treatment, the texture became soft without impairing the performance such as shrinkage resistance.

Claims (5)

セルロース系繊維含有織編物を液体アンモニア処理した後、樹脂加工剤を付与し、次いで120〜200℃、ニップ圧200〜300kgf/cm、速度5〜15m/分で熱カレンダー処理又は該熱カレンダー処理及び120〜170℃で熱処理を施し、最後に98℃以上150℃未満で熱水に浸漬して処理することを特徴とするセルロース系繊維含有織編物の加工方法。After processing the cellulosic fiber-containing textile fabric with the liquid ammonia, to grant resin finish, followed by 120 to 200 [° C., nip pressure 200~300kgf / cm, rate of 5 to 15 m / min by heat calendering or the heat calendering and 120 to 170 subjected to Netsusho management at ° C., the processing method of the cellulosic fiber-containing textile fabric characterized by immersing the treated hot water in less than last 98 ° C. or higher 0.99 ° C.. 樹脂加工剤を含む加工液が、更に架橋触媒及び架橋反応助剤を含有する請求項1記載の方法 The method according to claim 1, wherein the processing liquid containing the resin processing agent further contains a crosslinking catalyst and a crosslinking reaction aid . 樹脂加工剤を含む加工液が、更に目詰剤を含有する請求項1又は2記載の方法 The method according to claim 1 or 2, wherein the processing fluid containing the resin processing agent further contains a plugging agent . 熱水処理が、高圧液流染色機、高圧パドル染色機、高圧ドラム染色機、高圧ジッガー染色機又は高圧ビーム染色機によるものである請求項1、2又は3記載の方法 The method according to claim 1, 2 or 3, wherein the hot water treatment is performed by a high pressure liquid dyeing machine, a high pressure paddle dyeing machine, a high pressure drum dyeing machine, a high pressure jigger dyeing machine or a high pressure beam dyeing machine . 熱水処理の際、液中に柔軟剤を加えるようにした請求項1乃至4のいずれか1項記載の方法。The method according to any one of claims 1 to 4 , wherein a softening agent is added to the liquid during the hot water treatment.
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US6740126B2 (en) * 2000-02-15 2004-05-25 Strike Investments, Llc Method for the application of durable press finishes to textile components via the use of hydrophobic bleaching preparation
JP4739929B2 (en) * 2005-03-25 2011-08-03 三洋化成工業株式会社 Anti-shrinking agent for textiles
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