JP4593827B2 - Polarizing film manufacturing method and manufacturing apparatus - Google Patents

Polarizing film manufacturing method and manufacturing apparatus Download PDF

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Publication number
JP4593827B2
JP4593827B2 JP2001158078A JP2001158078A JP4593827B2 JP 4593827 B2 JP4593827 B2 JP 4593827B2 JP 2001158078 A JP2001158078 A JP 2001158078A JP 2001158078 A JP2001158078 A JP 2001158078A JP 4593827 B2 JP4593827 B2 JP 4593827B2
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polarizing film
stretching
film substrate
film
iodine
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JP2002350638A (en
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禎造 西
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NISHI INDUSTRY CO., LTD.
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NISHI INDUSTRY CO., LTD.
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Description

【0001】
【発明の属する技術分野】
本発明は、ポリビニールアルコール(以下、『PVA』と省略することがある。)からなる偏光フィルムの製造技術に係わる。特に、液晶表示用途に供し得る精度の高い偏光フィルムの製造技術に関する。
【0002】
【従来の技術】
従来から偏光フィルムとして、PVAの一軸又は二軸延伸フィルムであって、ヨウ素を吸着させたものがよく知られている。また、PVAフィルムに二色性染料を吸着せしめ、配向させた二色性染料配向フィルムも一般によく知られている。
【0003】
ところで、PVA偏光フィルムを製造するに際し、乾式延伸法と湿式延伸法との2種類の延伸方法に大別でき、実際にも双方の技術が採択されているが、これらは一長一短であると考えられてきている。即ち、乾式延伸の場合にはPVA分子間の水素結合をある程度緩和して一軸延伸際のネックイン現象を抑制することができるので、フィルムの厚さ斑の発生を抑え、光透過率の均一性が期待出来る利点が指摘できる。もっとも、乾式延伸には、水素結合を緩和することにより、維持軸延伸に際して分子間のズレが生じ、延伸倍率を高めた割合には偏光性能(分子配向)が高まらず、偏光性を更に高めようと延伸倍率を上げるとフィルムの破断が発生する危険を伴いやすい。
【0004】
PVAフィルムの湿式延伸法にも、長所と短所とがあり、上述の乾式延伸法の利点は概ね湿式延伸法の短所、乾式延伸法の短所は概ね湿式延伸法の長所であると言えよう。
【0005】
本発明は、PVA偏光フィルムの製造に際し、乾式延伸法と湿式延伸法の長所を夫々生かす、言い換えれば両者の問題点を極力回避できる延伸技術を開発することを課題とするものである。
【0006】
【従来技術の問題点】
従来技術として、乾式延伸方法によるものとして、特開平8−240715号公報には重合度2000〜10000のPVAからなるフィルムを乾式で一軸延伸し、染色後70〜85℃の硼酸含有水溶液浸漬処理する方法が開示されているが、このPVA偏光フィルムは機械的強度に劣り、偏光板に形成する際や、偏光板として使用する際に、破断が起こりやすい問題点があった。ホウ素化合物でPVA偏光フィルムを後処理する特開平4−215603号公報記載の方法では、偏光板に面内のコントラスト斑が生じるので、光学特性に劣る問題が解消できない。
【0007】
このように、乾式延伸法では延伸倍率を高めても、さほど分子配向が高まらず、偏光性を更に高めようと延伸倍率を上げるとフィルムの破断が発生するため、安定した製造方法とは言えない問題点が存在した。
【0008】
本発明は、この解決方法として、乾式延伸法と湿式延伸法とを組み合わせる手段を採るものであるが、単なる折衷方式ではなく、両者の利点を生かそうとする技術である。殊に、液晶用途に要求される高精度なTFF−LCD用には、コントラストの良好な性能を備えた偏光フィルムが望ましいので、これに応えられるPVAフィルムの製造技術を提供できなければならない。
【0009】
本発明では製造方法として、基本的に、先ず、気中延伸(気相中で延伸すること。乾燥状態で実施する乾式延伸や水浴中で行う液相中延伸と区別するため「気中延伸」と称することとする。)とを施し、継いで偏光性能を備えるべくヨウ素錯塩色剤を染着処理(染料定着処理を含む)し、更に水、水溶液又はアルコール類等の膨潤剤の存在下で湿式延伸を施し、乾燥手段によって膨潤剤を除去し、要すれば、補色処理や延伸定着処理を加え、偏光フィルムの製造を完了する。
【0010】
染着処理が施されてヨウ素を含んだPVAフィルムを気中延伸することも可能であるが、この場合には、染着処理工程、乾式延伸工程と続くこととなり、従来技術の延伸中に充分な分子配列が起こらない問題を解決することは難しいので奨められない。
【0011】
従って、本発明では、気中延伸によりPVAフィルムを先ずある程度分子配列せしめ、以後沃素等の偏光剤を含んだPVAフィルムを湿式延伸することにより構成される。この製造手法は、偏光フィルムとしての性能を高め、厚み斑及び分子配向斑の少ない高品質フィルムが得易くなることを知見した結果に基くものである。
【0012】
なお、偏光フィルムを得た後、実際の生産では完成された状態で出荷することが要請される。そこで、液晶表示セルにすぐに貼付できるように、偏光フィルムには、引き続いて、トリアセテートフィルムによりPVAフィルムをラミネート処理するラミネート処理工程、粘着層を貼付けて液晶表示セルと貼着出来るように施す粘着層塗工処理工程、及び所定の仕様サイズにカッティングする仕上げする工程と巻取工程とが加わる。
【0013】
更に、用途を加味して、補説すると、液晶表示セル用には高度のコントラストを有する偏光板が要求されるが、この対策として、本発明のPVAフィルムの気中延伸を先ず施し、継いで膨潤処理に際し、単なる水に換えて水に硼酸を加えると膨潤処理が効果的となる事実が知られている(特開平10−153709号公報参照)が、この技術を利用することが本発明でも可能である。また膨潤処理の後にヨウ素染色処理を施し、次いで湿式延伸を施すことが工程的に好ましい。
【0014】
偏光フィルムとして、適切な分子配向を備え、斑の無い均一な製品を得るためには、気中延伸と湿式延伸とを巧みに組み合わせる必要がある。このことによって始めて高品質な製品を効率的に、合理的に製造できるものである。従来技術ではともすれば、品質を重視して効率の良くない湿式延伸を採用するか、生産効率や低コストを重視して乾式延伸法を選択する傾向があったが、乾式の方が優れているか否かを論ずるのではなく、両者の特質を理解し、効果的に組み合わせると、従来技術にない優れた性能を引出すことが可能となるのである。
【0015】
【発明が解決しようとする課題】
ポリビニールアルコールからなるフィルムを気中熱延伸する手段は、第1にフィルムに管理された温度湿度を施すことである。PVAフィルムは親水性ポリマーであるから水に対し極めて敏感である。水滴が存在する雰囲気では、水中に浸漬した場合と異なり、フィルム表面に不均一に水分子が付着し、水素結合の緩和状態が不規則的になる。この状態でフィルムが張力を受けると不均一性は一層助長される。この現象を回避するために、本願発明ではフィルム表面に水滴、結露が全くない雰囲気にフィルムを誘導しなければならない。通常親水性フィルム重合体はその表面において結露が観測されることはない。それは水滴が直ちに吸収されるからである。しかし、如上の通り、水滴が存すると不均一な膨潤作用が生じることになる。この水滴回避に極めて注意をする必要があり、本願発明を実施する上で、重要な指針となる。
【0016】
そこで、フィルム等の表面には全く結露がない状態とするためには、気中延伸装置内外(周囲)を予め調湿加熱(未飽和蒸気下で予備加熱)する。
【0017】
その際相対湿度を80−90−95%程度に段階的に維持して加熱する。また延伸操作は、延伸室において、PVAフィルムを調湿装置と同一条件乃至より乾燥した条件に曝し、直ちに所定の倍率となるように延伸する。
【0018】
なお、延伸装置内外は、延伸ロール群はもとより、蒸気浴槽の天井、壁等にも結露がまったく生じないように、延伸ロール群、蒸気浴槽の天井及び壁等の周囲の温度を蒸気温度よりも0.5−5℃高く維持し、精密に温度制御する。
【0019】
更に蒸気雰囲気(浴)から出る直後の位置において、延伸フィルムを乾燥空気により冷却して、冷却・放熱に伴う結露の生成を抑制するような処理、例えば乾燥空気吹付け手段を設けることが好ましい。
【0020】
過加熱を完全に回避することは、高度の延伸倍率で延伸されたフィルムでは破断し易い性質を伴うため、必要な処理となる場合が多い。従って設備上は過加熱が生じないように温度制御に留意した設備を設ける。
【0021】
更に、張力調整を完全に行うことことも要求される場合がある。上述の高度に延伸されたフィルムでは張力が高すぎるとフィルムが破断し易くなる。そこで例えば、中間にロール軸間距離が変動できる緩衝手段である、例えばダンサーロールを設ける等の工夫が求められる。
【0022】
本発明では、PVAフィルムに先ず気中延伸を施し、ついで膨潤処理、染着処理を施し、更に湿式延伸を施す工程を、通常、この順に実施するものである。この延伸手段を施すことにより高機能、高品質の偏光フィルムが得られる。
【0023】
【課題を解決する手段】
上述の課題を達成するために、請求項1に係る発明は、ポリビニールアルコール樹脂よりなる偏光フィルム基材を膨潤処理する工程と、膨潤処理された偏光フィルム基材をヨウ素染色する工程と、ヨウ素染色された偏光フィルム基材を1軸延伸する延伸工程と、延伸工程を経た偏光フィルム基材にヨウ素染色剤を定着させる色剤定着工程と、色剤定着工程を経た偏光フィルム基材を水洗する水洗工程と、水洗工程を経た偏光フィルム基材を乾燥せしめる乾燥工程とを含むポリビニールアルコール樹脂よりなる液晶セル用偏光フィルムの製造方法である。請求項1の発明では、延伸工程としてフィルム表面には全く結露がない状態を保って、未飽和蒸気下で予備加熱して相対湿度を80−95%程度に維持し、次いで同雰囲気乃至より乾燥条件において、偏光フィルム基材に直ちに延伸を施すことからなる気中延伸法を特徴とする。
【0024】
請求項2に係る発明は、液晶表示セル用に適する高度のコントラストを有する偏光板を得るために、請求項1に記載の液晶セル用偏光フィルムの製造に際し、気中延伸の前か又は後に実施する工程であって、フィルム基材の水洗(膨潤)工程において、硼酸水溶液を使用して水洗(膨潤)処理を施すことを特徴とする。気中延伸されたフィルム基材に硼酸を含む水洗(膨潤)処理を施すと、水中延伸のみを施された従来型フィルムを硼酸水溶液水洗(膨潤)処理したものよりも、一段と優れたコントラストを持つ偏光フィルムが得られる効果がある。
【0025】
請求項3に係る発明は、液晶表示用には高度のコントラストを有する偏光板を得るために、請求項1に記載された液晶表示セル用偏光フィルムの製造において、水洗(膨潤)工程に沃化カリ水溶液を使用して水洗(膨潤)処理を施すことを特徴とする。この場合も水洗(膨潤)工程の前に気中延伸を済ませる方が望ましいが、勿論気中延伸工程の後に水洗処理しても差し支えない。気中延伸は、延伸に際しネックインが小さく、フィルム基材の幅方向における分子配向の状態が中心付近と両端部とに大きな差異がないので、この結果均質な偏光板が得られる。本発明における気中延伸されたフィルムの均質性は、水浴延伸のみを施されたフィルム基材と較べるとき顕著な相違点であり、気中延伸を施されたフィルムの優れた点である。このように本発明によれば高度のコントラストを有する偏光フィルムが得られる利点がある。
【0026】
請求項4の発明は、気中1軸延伸が実施できる製造装置であって、ポリビニールアルコール樹脂よりなる偏光フィルム基材を膨潤処理する手段と、膨潤処理された偏光フィルム基材をヨウ素染色する染色手段と、ヨウ素染色された偏光フィルム基材を1軸延伸する延伸手段と、延伸工程を経た偏光フィルム基材にヨウ素染色剤を定着させる色剤定着手段と、色剤定着工程を経た偏光フィルム基材を水洗する水洗手段と、水洗工程を経た偏光フィルム基材を乾燥せしめる乾燥手段と、を含むポリビニールアルコール樹脂よりなる液晶用セルの製造手段において、延伸手段が、偏光フィルム基材と接する全ての手段に亘り、その表面に全く結露がない状態を保つことができる水蒸気温度よりも少なくとも0.5℃高温に維持し得る加熱手段を備え、偏光フィルム基材を未飽和蒸気下で予備加熱して乾燥(相対湿度を80−95%程度に維持して加熱)する手段と、偏光フィルム基材を直ちに延伸し得る手段とを備えたことを特徴とする。
【0027】
請求項5に係る発明は、製造装置が、気中1段延伸が可能であって、その延伸倍率は1:2〜8の範囲及び延伸フィルムを湿式再延伸するときの延伸比率は1:1.5〜5.0程度となる延伸条件を満たす延伸装置を備え、しかも気中延伸温度は60〜120℃の範囲において、所定の温度に精度良く維持でき、常圧(蒸気が浴装置外に放出できる程度に高圧の場合をも含む)を保持できる気中延伸手段を備えている点に特徴を有する。
【0028】
【実施の態様】
以下に、図面を参照して本発明の製造方法及び製造装置を説明する。
【0029】
図1に本発明に係るPVA偏光フィルムの製造装置の概略を示す。この装置の配列は、ヨウ素を吸着させずにPVAフィルムを先ず気中延伸する場合の実施態様を示しているが、勿論ヨウ素を吸着させて気中又は湿式延伸する実施態様も想定される。
【0030】
図1では未延伸状態のPVAフィルムを調湿する工程から始まる。巻出機からミルロール(未延伸状態のPVAフィルム)を巻き出して調湿するが、巻出機にミルロールを架ける前に、ミルロールが入荷された後に調湿槽〈調湿倉庫〉において所定時間に亘り調湿することも可能である。本発明において、この調湿工程はクリーンルーム(クリーンユニット)における脱塵埃処理を兼ねている。勿論、脱塵埃処理を調湿槽〈調湿倉庫〉において施すことも可能である。
【0031】
調湿処理を経たPVAフィルムは、延伸工程に導かれ、ここで所定の条件で延伸配向が施される。気中延伸処理はフィルム幅方向における縮み(ネックイン)が少なく、幅方向における厚み斑も少なくなる利点があるので、延伸処理の初期の段階で実施する本発明方法は優れている。
【0032】
気中延伸を施されたPVA延伸フィルムは、次に膨潤工程において水又は膨潤剤の存在下で膨潤処理される。この処理でPVA延伸フィルムは水浴槽に完全に浸漬される。そして、膨潤処理を施されたPVA延伸フィルムはヨウ素、ヨウ化カリ水溶液(ヨウ素/ヨウ化カリ/水の組成)において染色される。
【0033】
染色されたPVA延伸フィルムは水洗され未反応(未染色)の状態の遊離した色剤等を除く作業が施される。ヨウ素色剤がPVA分子(フィルム)に定着された状態で、今度は湿式延伸が施される。この延伸処理によって偏光フィルムが得られる。
【0034】
偏光フィルムは再度の水洗処理が施された後、乾燥機を経て乾燥された状態で巻き取られる。
【0035】
図2は全体の工程を示すフローチャートである。上述の気中延伸されたPVAフィルムが、ヨウ素色剤により染色された状態で湿式延伸された偏光フィルムとなり、巻き取られるか、セルローズトリアセテートのような透明度の高いフィルムによりラミネート処理されるラミネート処理工程、粘着剤が塗布される粘着層塗工工程、及び所望の寸法にカッティングされる仕上工程を併記したものである。
【0036】
図3は、乾式延伸装置を少し詳しく説明した説明図である。巻き出されたミルロール21は、脱塵埃処理され、管理された温度湿度の雰囲気を作り出すクリーンユニット22、23及び24において調湿される。次に、フィルムは延伸装置に導かれて、ここでニップローラ25と延伸高速ローラ27との周速度の比率を適宜設定することにより、1対2〜8程度の範囲(延伸倍率)において延伸される。この際の延伸温度は60〜120℃の範囲が選択されるが、フィルムを形成するPVAの分子量〈重合度〉が高い材料では、一般に、高めの延伸温度を選択する。
【0037】
フィルムが導入される延伸ゾーン25,26,27は、延伸工程としてフィルム表面には全く結露がない状態が保たれており、フィルムは未飽和蒸気下で予備加熱して乾燥(相対湿度を80−95%程度に維持されるように加熱)され、継いで偏光フィルム基材を蒸気浴槽36において飽和蒸気に曝されながら、直ちに延伸が施される。未延伸フィルムが導入される入口部34及び延伸フィルムが導出される出口部35は、それぞれシールボックスが配備されている。
【0038】
このようにPVAフィルムを周速度の異なるロール間で一軸延伸するに際し、先ずフィルムが濡れない状態で60〜120℃の気中熱延伸を施す。例えば、完全乾式加熱を施し、フィルムや装置に結露がない状態とし、乾燥予熱(未飽和蒸気下で予備加熱する)、調湿24、25(相対湿度を80−95%程度に維持して加熱)、同雰囲気条件で直ちに延伸するものである。この延伸中では、延伸フィルムの出口直前35に乾燥空気によりシールし、冷却に伴う結露の生成を抑制する。更に、過加熱を完全に回避すること及び張力調整を完全に行うことが附加される。乾式延伸されたPVAフィルムは引続き膨潤処理、染色、湿式延伸を経て偏光フィルムとなる。一群のロール26,26・・・・・・は結露が発生しないように延伸温度よりも少なくとも0.5℃〜5℃高い表面温度に維持される。
【0039】
本発明の乾式延伸は図3のように一旦巻取機32で巻き取ることが出来る。その際、PVA延伸フィルムに添うように、別なフィルムをロール31から引出してローラ27、28を介して重ね巻きして補助フィルムと同時に巻き上げることも可能である。
【0040】
連続して、図1に示したような装置により、PVAフィルムを製造することが出来るのは言うまでもない。
【0041】
このように本発明では、気中延伸装置及びクリーンユニットを含む調湿装置を除き、従来技術をほぼ踏襲している。更に補説すると、加熱ローラの予熱範囲として、50〜120℃を設定でき、また設定温度を0.5℃の精度で所望温度とすることが仕様となる。所定の延伸温度に到達するまでの加熱時間はクリーンユニットの滞留時間を調節することか、フィルムの走行速度を調整することで達成できる。
【0042】
なお、延伸後のフィルムを直ちに冷却することが分子の配向状態を維持するうえで望ましいが、結露防止も必要であり、乾燥空気を用いて出口部をシールボックスで覆うことが有効である。同様な効果は張力管理においても達成できる。
【0043】
【実施例】
<参考例>
延伸条件と物性について説明する。
【0044】
原料ポリビニルアルコールフィルムとして、クラレ株式会社製「ビニロン(登録商標)」フィルムVF-XS#7500を用いた。
【0045】
染色液として、ヨウ素水溶液(ヨウ素/ヨウ化カリ/水=0.05/5/100の組成)を用いた。
【0046】
偏光度の測定は日本電子機械工業規格(EIJL)LD−201−1983に準拠し、延伸フィルムを乾燥した後分光光度計を用い偏光板内の光線透過率を5点測定し、算出した。
【0047】
染色後の洗浄は、硼(ホウ)酸(HBO3)を1%含有する25℃の純水で行った。
【0048】
湿式延伸はホウ酸(HBO3)を1%含有する30℃の純水中、送り速度3m/分であり、延伸倍率に応じ巻取り側のロール速度を上げて延伸した。
【0049】
ビニロンフィルムを図1に示した気中延伸装置を用い、調湿及び延伸雰囲気条件を80℃、93%相対湿度状態として、送り速度1m/分、引取り速度6m/分で、6.0倍に延伸した。継いで、染色し、更に純水で洗浄した。引き続き、50℃の温風で5分間乾燥した後、延伸フィルムについて光学特性の測定を実施した。
【0050】
この延伸フィルムの光線透過率は42.2%、偏光度は99.9%、光線透過率のフィルム面内バラツキは0.04%であった。
<実施例1>
参考例で得た6倍延伸フィルムを再度染色し、純水で洗浄後、再び1.7倍に湿式延伸し、継いで50℃の温風で5分間乾燥した。得られた再延伸フィルムの物性値は、光線透過率は43.1%、偏光度は99.9%、光線透過率のフィルム面内バラツキは0.21%であった。
<実施例2>
参考例で調湿及び延伸装置の内部温度を70℃、95%相対湿度状態を維持し、引取り速度3m/分(延伸倍率3倍)として延伸し、更に2.5倍湿式延伸した。得られた再延伸フィルムの物性値は、光線透過率は43.3%、偏光度は99.9%、光線透過率のフィルム面内バラツキは0.40%であった。
【0051】
【発明の効果】
気中延伸と湿式延伸の双方の利点を引出したPVAフィルムの製造技術であるから、一軸延伸に際して、ネックイン現象を抑制することができるので、フィルムの厚さ斑の発生を抑え、光透過率の均一性が優れている効果を奏する。
【0052】
湿式延伸を併用しているので、延伸倍率を高めることが可能で、偏光性能(分子配向)を充分に高めることが出来る。しかも乾式延伸方のようなフィルムの破断が発生する懸念もなく、安定した製造が可能となる効果が奏される。
【0053】
更に、気中延伸においてネックイン現象を抑制できるので、フィルムの幅方向での分子配向状態の均一性が優れ、高度のコントラストを備えた偏光フィルムが得られる。
【図面の簡単な説明】
【図1】本発明に係るPVA偏光フィルムの製造装置の概略を示す。
【図2】本発明を含む全体の工程を示すフローチャートである。
【図3】本発明に係るPVA偏光フィルムの気中延伸装置の説明図である。
【符号の説明】
20 気中延伸工程
21 巻出機
22 調湿装置
23 クリーンユニット
25 低速側延伸ローラ
26 加熱ローラ
27 高速側延伸ローラ
28 ラミネート用ローラ
29 ガイドローラ
30 気中延伸浴(延伸ゾーン)
31 異種フィルム供給ロール
32 巻取機
34 入口部シールボックス
35 出口部シールボックス
36 スチーミング装置
37 天井加熱結露防止装置
38 壁面加熱結露防止装置
42 膨潤工程
44 染色工程
46 洗浄・定着工程
48 湿式延伸工程
52 第2洗浄工程
54 乾燥工程
62 ラミネート処理工程
64 粘着層貼着肯定
66 仕上工程
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a technique for producing a polarizing film made of polyvinyl alcohol (hereinafter sometimes abbreviated as “PVA”). In particular, the present invention relates to a technique for producing a highly accurate polarizing film that can be used for liquid crystal display applications.
[0002]
[Prior art]
Conventionally, as a polarizing film, a uniaxial or biaxially stretched film of PVA, which adsorbs iodine, is well known. A dichroic dye oriented film obtained by adsorbing and orienting a dichroic dye on a PVA film is generally well known.
[0003]
By the way, when manufacturing a PVA polarizing film, it can be roughly divided into two types of stretching methods, a dry stretching method and a wet stretching method, and both techniques are actually adopted, but these are considered to be merits and demerits. It is coming. In other words, in the case of dry stretching, the hydrogen bonds between PVA molecules can be relaxed to some extent to suppress the neck-in phenomenon during uniaxial stretching, thus suppressing the occurrence of film thickness unevenness and the uniformity of light transmittance. The advantages that can be expected can be pointed out. However, in the case of dry stretching, by relaxing the hydrogen bond, an intermolecular shift occurs during the sustaining axis stretching, and the polarization performance (molecular orientation) does not increase at a ratio of increasing the stretching ratio, so that the polarization is further improved. If the draw ratio is increased, the film is likely to break.
[0004]
The wet stretching method for PVA film also has advantages and disadvantages. The advantages of the dry stretching method described above are generally the disadvantages of the wet stretching method, and the disadvantages of the dry stretching method are generally the advantages of the wet stretching method.
[0005]
An object of the present invention is to develop a stretching technique that makes the best use of the advantages of the dry stretching method and the wet stretching method in manufacturing the PVA polarizing film, in other words, avoids both problems as much as possible.
[0006]
[Problems of the prior art]
As a conventional technique, according to a dry stretching method, Japanese Patent Application Laid-Open No. 8-240715 discloses a film made of PVA having a polymerization degree of 2000 to 10,000 is uniaxially stretched in a dry manner and is immersed in an aqueous solution containing boric acid at 70 to 85 ° C. after dyeing. Although a method has been disclosed, this PVA polarizing film is inferior in mechanical strength, and has a problem that breakage tends to occur when it is formed on a polarizing plate or used as a polarizing plate. In the method described in JP-A-4-215603 in which a PVA polarizing film is post-treated with a boron compound, in-plane contrast spots are generated on the polarizing plate, and thus the problem of poor optical characteristics cannot be solved.
[0007]
Thus, in the dry stretching method, even if the stretching ratio is increased, the molecular orientation does not increase so much, and if the stretching ratio is increased to further increase the polarization, the film breaks, so it cannot be said to be a stable production method. There was a problem.
[0008]
The present invention employs a means for combining the dry stretching method and the wet stretching method as a solution to this problem, but it is not a simple compromise method, but a technique that takes advantage of both. In particular, for a high-precision TFF-LCD required for liquid crystal applications, a polarizing film having good contrast performance is desirable, and it is necessary to provide a PVA film manufacturing technique that can meet this demand.
[0009]
In the present invention, as a production method, basically, first, stretching in the air (stretching in the gas phase. In order to distinguish it from dry stretching performed in a dry state and stretching in liquid phase performed in a water bath, “in-air stretching” is used. In the presence of a swelling agent such as water, an aqueous solution, or alcohols, the iodine complex salt colorant is dyed (including a dye fixing process) to provide polarization performance. Wet stretching is performed, the swelling agent is removed by a drying means, and if necessary, complementary color processing and stretching fixing processing are added to complete the production of the polarizing film.
[0010]
It is also possible to stretch in the air a PVA film containing iodine after being dyed, but in this case, it will be followed by the dyeing process and the dry stretching process, which is sufficient during the stretching of the prior art. It is not recommended because it is difficult to solve the problem that the correct molecular arrangement does not occur.
[0011]
Therefore, in the present invention, the PVA film is first molecularly aligned to some extent by stretching in the air, and thereafter, the PVA film containing a polarizing agent such as iodine is wet-stretched. This manufacturing method is based on the result of finding that it is easy to obtain a high-quality film with improved thickness as a polarizing film and less thickness spots and molecular orientation spots.
[0012]
In addition, after obtaining a polarizing film, it is requested | required to ship in the completed state in actual production. Therefore, in order to be able to be applied immediately to the liquid crystal display cell, the polarizing film is subsequently subjected to a laminating process in which a PVA film is laminated with a triacetate film, an adhesive layer is applied so that the adhesive layer can be attached to the liquid crystal display cell. A layer coating treatment process, a finishing process for cutting to a predetermined specification size, and a winding process are added.
[0013]
Furthermore, taking the application into consideration, a supplementary polarizing plate for liquid crystal display cells is required, but as a countermeasure against this, the PVA film of the present invention is first stretched in the air and then continued. In the swelling treatment, it is known that the swelling treatment is effective when boric acid is added to water instead of mere water (see Japanese Patent Laid-Open No. 10-153709). Is possible. In addition, it is preferable in terms of process that an iodine dyeing process is performed after the swelling process and then wet stretching is performed.
[0014]
In order to obtain a uniform product having appropriate molecular orientation and no spots as a polarizing film, it is necessary to skillfully combine air stretching and wet stretching. Only in this way can a high-quality product be produced efficiently and rationally. In the prior art, there was a tendency to use inefficient wet stretching with emphasis on quality, or to select a dry stretching method with emphasis on production efficiency and low cost, but the dry method is better. Rather than discussing whether or not it is, understanding the characteristics of both and combining them effectively makes it possible to bring out superior performance not found in the prior art.
[0015]
[Problems to be solved by the invention]
The means for hot stretching the film made of polyvinyl alcohol in the air is to first apply a controlled temperature and humidity to the film. Since PVA film is a hydrophilic polymer, it is extremely sensitive to water. In an atmosphere where water droplets are present, unlike when immersed in water, water molecules adhere nonuniformly to the film surface, and the relaxed state of hydrogen bonds becomes irregular. In this state, when the film is subjected to tension, the non-uniformity is further promoted. In order to avoid this phenomenon, in the present invention, the film must be guided to an atmosphere where there is no water droplets or condensation on the film surface. Usually, no condensation is observed on the surface of the hydrophilic film polymer. This is because water droplets are absorbed immediately. However, as described above, the presence of water droplets causes a non-uniform swelling action. It is necessary to pay particular attention to avoiding water droplets, and this is an important guideline for implementing the present invention.
[0016]
Therefore, in order to make the surface of the film or the like not dewed at all, the inside and outside (the surroundings) of the air stretching apparatus are preliminarily humidified (preheated under unsaturated steam).
[0017]
At that time, the relative humidity is maintained in steps of about 80-90-95% and heated. In the stretching operation, in the stretching chamber, the PVA film is exposed to the same conditions as the humidity control apparatus or more dried conditions, and immediately stretched to a predetermined magnification.
[0018]
In addition, the temperature around the stretching roll group, the ceiling of the steam bath, and the wall of the stretching tub is not higher than the steam temperature so that condensation does not occur at all on the ceiling and wall of the steam bath as well as the stretching roll group. Maintain 0.5-5 ° C higher and control temperature precisely.
[0019]
Furthermore, it is preferable to provide a treatment, for example, a dry air spraying means, for cooling the stretched film with dry air at a position immediately after coming out of the steam atmosphere (bath), for example, to suppress the formation of condensation accompanying cooling and heat dissipation.
[0020]
Completely avoiding overheating is often a necessary treatment because a film stretched at a high stretch ratio is easily broken. Therefore, facilities that pay attention to temperature control are provided so that overheating does not occur.
[0021]
Further, it may be required to completely adjust the tension. In the above-described highly stretched film, if the tension is too high, the film tends to break. Therefore, for example, a device such as a dancer roll, which is a buffer means that can change the distance between the roll axes in the middle, is required.
[0022]
In the present invention, the steps of first subjecting the PVA film to air stretching, then subjecting it to swelling treatment and dyeing treatment, and further subjecting it to wet stretching are usually carried out in this order. By applying this stretching means, a high-functional and high-quality polarizing film can be obtained.
[0023]
[Means for solving the problems]
In order to achieve the above-described problems, the invention according to claim 1 includes a step of swelling a polarizing film substrate made of polyvinyl alcohol resin, a step of iodine-staining the polarizing film substrate subjected to swelling treatment, and iodine. A stretching step for uniaxially stretching the dyed polarizing film substrate, a colorant fixing step for fixing an iodine staining agent to the polarizing film substrate that has undergone the stretching step, and a water washing of the polarizing film substrate that has undergone the coloring agent fixing step It is a manufacturing method of the polarizing film for liquid crystal cells which consists of a polyvinyl alcohol resin including the washing process and the drying process which dries the polarizing film base material which passed through the washing process. In the first aspect of the present invention, the film surface is kept free of condensation as the stretching step, preheated under unsaturated steam to maintain a relative humidity of about 80-95%, and then the same atmosphere or more dried. In the conditions, it is characterized by an in-air stretching method comprising immediately stretching the polarizing film substrate.
[0024]
In order to obtain a polarizing plate having a high contrast suitable for a liquid crystal display cell, the invention according to claim 2 is carried out before or after stretching in the air during the production of the polarizing film for a liquid crystal cell according to claim 1. In the water washing (swelling) step of the film substrate, a water washing (swelling) treatment is performed using an aqueous boric acid solution. When the film substrate that has been stretched in air is subjected to a washing (swelling) treatment containing boric acid, it has a contrast superior to that obtained by washing (swelling) a conventional film that has been stretched in water only with a boric acid solution. There is an effect that a polarizing film is obtained.
[0025]
According to a third aspect of the present invention, in order to obtain a polarizing plate having a high contrast for a liquid crystal display, in the production of the polarizing film for a liquid crystal display cell according to the first aspect, the water washing (swelling) step is iodinated. A water washing (swelling) treatment is performed using an aqueous potassium solution. In this case as well, it is desirable that the air stretching is completed before the water washing (swelling) step, but of course, water washing treatment may be performed after the air stretching step. In the air stretching, the neck-in is small during stretching, and the state of molecular orientation in the width direction of the film base material is not greatly different between the center and both ends, so that a uniform polarizing plate is obtained as a result. The homogeneity of the film stretched in the air in the present invention is a significant difference when compared with a film substrate subjected only to water bath stretching, and is an excellent point of the film stretched in the air. Thus, according to the present invention, there is an advantage that a polarizing film having a high degree of contrast can be obtained.
[0026]
The invention of claim 4 is a manufacturing apparatus capable of carrying out uniaxial stretching in the air, and means for swelling a polarizing film substrate made of polyvinyl alcohol resin, and iodine-staining the swollen polarizing film substrate Dyeing means, stretching means for uniaxially stretching the iodine-stained polarizing film substrate, colorant fixing means for fixing the iodine dyeing agent to the polarizing film substrate that has undergone the stretching process, and polarizing film that has undergone the colorant fixing process In a means for producing a liquid crystal cell comprising a polyvinyl alcohol resin, the stretching means is in contact with the polarizing film base material, including a water washing means for washing the base material with water and a drying means for drying the polarizing film base material that has undergone the water washing step. Heating means capable of maintaining at least 0.5 ° C. higher than the water vapor temperature capable of keeping the surface completely dew-free over all means A means for pre-heating the polarizing film substrate under unsaturated steam and drying (heating while maintaining the relative humidity at about 80-95%); and a means for immediately stretching the polarizing film substrate. Features.
[0027]
In the invention according to claim 5, the production apparatus can perform one-stage stretching in the air, the stretching ratio is in the range of 1: 2 to 8, and the stretching ratio when the stretched film is wet-stretched is 1: 1. comprising a stretching satisfies stretching apparatus comprising about .5~5.0, moreover in the range of the stretching temperature is 60 to 120 ° C. in air, accurately be maintained at a predetermined temperature, atmospheric pressure (outside vapor bath apparatus It is characterized in that it has an air stretching means that can maintain a high pressure (including the case of a high pressure that can be released).
[0028]
Embodiment
Below, the manufacturing method and manufacturing apparatus of this invention are demonstrated with reference to drawings.
[0029]
FIG. 1 shows an outline of an apparatus for producing a PVA polarizing film according to the present invention. The arrangement of this apparatus shows an embodiment in which a PVA film is first stretched in the air without adsorbing iodine, but of course, an embodiment in which iodine is adsorbed and in the air or wet stretching is also envisaged.
[0030]
In FIG. 1, the process starts from the step of conditioning the unstretched PVA film. The mill roll (unstretched PVA film) is unwound from the unwinder to adjust the humidity, but before the mill roll is mounted on the unwinder, after the mill roll is received, the humidity control tank <humidity control warehouse> It is also possible to adjust the humidity over a wide range. In the present invention, this humidity control step also serves as dust removal processing in a clean room (clean unit). Of course, the dust removal treatment can be performed in a humidity control tank <humidity control warehouse>.
[0031]
The PVA film that has undergone the humidity conditioning treatment is guided to a stretching process, where it is stretched and oriented under predetermined conditions. In-air stretching is advantageous in that the shrinkage (neck-in) in the film width direction is small and the thickness unevenness in the width direction is small, so that the method of the present invention carried out at the initial stage of the stretching process is excellent.
[0032]
The PVA stretched film that has been stretched in the air is then subjected to a swelling treatment in the presence of water or a swelling agent in a swelling step. By this treatment, the PVA stretched film is completely immersed in the water bath. The PVA stretched film that has been subjected to the swelling treatment is dyed in iodine, potassium iodide aqueous solution (composition of iodine / potassium iodide / water).
[0033]
The dyed PVA stretched film is washed with water and subjected to an operation to remove the unreacted (undyed) free colorant and the like. With the iodine colorant fixed to the PVA molecule (film), wet stretching is performed this time. A polarizing film is obtained by this stretching treatment.
[0034]
The polarizing film is subjected to a water washing treatment again and then wound up in a dried state through a dryer.
[0035]
FIG. 2 is a flowchart showing the entire process. The above-mentioned air-stretched PVA film becomes a wet-stretched polarizing film dyed with an iodine colorant, and is wound or laminated with a highly transparent film such as cellulose triacetate. The adhesive layer coating process in which an adhesive is applied, and the finishing process in which a desired size is cut are shown.
[0036]
FIG. 3 is an explanatory diagram illustrating the dry stretching apparatus in some detail. The unrolled mill roll 21 is dedusted and conditioned in clean units 22, 23 and 24 that create an atmosphere of controlled temperature and humidity. Next, the film is guided to a stretching apparatus, where it is stretched in a range of about 1 to 2 (stretching ratio) by appropriately setting the ratio of the peripheral speeds of the nip roller 25 and the stretching high-speed roller 27. . The stretching temperature at this time is selected in the range of 60 to 120 ° C., but a higher stretching temperature is generally selected for a material having a high molecular weight <polymerization degree> of PVA forming the film.
[0037]
In the stretching zones 25, 26, and 27 into which the film is introduced, the film surface is kept free from condensation as a stretching process, and the film is preheated and dried (with a relative humidity of 80− under an unsaturated vapor). Then, the polarizing film substrate is immediately stretched while being exposed to saturated steam in the steam bath 36. A seal box is provided in each of the inlet 34 where the unstretched film is introduced and the outlet 35 where the stretched film is led out.
[0038]
Thus, when uniaxially stretching a PVA film between rolls having different peripheral speeds, first, in-air hot stretching at 60 to 120 ° C. is performed in a state where the film is not wet. For example, complete dry heating is performed so that the film or device is not condensed, preheating for drying (preheating under unsaturated steam), humidity conditioning 24, 25 (relative humidity is maintained at about 80-95% and heating is performed. ), And stretched immediately under the same atmospheric conditions. During this stretching, sealing is performed with dry air 35 just before the exit of the stretched film to suppress the formation of condensation due to cooling. Furthermore, it is added that complete avoidance of overheating and complete tension adjustment. The dry stretched PVA film is subsequently subjected to swelling treatment, dyeing and wet stretching to become a polarizing film. The group of rolls 26, 26,... Are maintained at a surface temperature that is at least 0.5 ° C. to 5 ° C. higher than the stretching temperature so that condensation does not occur.
[0039]
The dry stretching of the present invention can be once wound up by a winder 32 as shown in FIG. At that time, it is also possible to draw another film from the roll 31 so as to follow the PVA stretched film, and to wrap the film through the rollers 27 and 28 and wind it simultaneously with the auxiliary film.
[0040]
Needless to say, the PVA film can be continuously produced by the apparatus shown in FIG.
[0041]
As described above, the present invention substantially follows the conventional technology except for the humidity control apparatus including the air stretching apparatus and the clean unit. As a further explanation, the preheating range of the heating roller can be set to 50 to 120 ° C., and the setting temperature is set to a desired temperature with an accuracy of 0.5 ° C. The heating time until reaching the predetermined stretching temperature can be achieved by adjusting the residence time of the clean unit or adjusting the running speed of the film.
[0042]
Although it is desirable to immediately cool the stretched film in order to maintain the molecular orientation, it is also necessary to prevent condensation, and it is effective to cover the outlet with a seal box using dry air. Similar effects can be achieved in tension management.
[0043]
【Example】
<Reference example>
Drawing conditions and physical properties will be described.
[0044]
As a raw material polyvinyl alcohol film, Kuraray Co., Ltd. “Vinylon (registered trademark)” film VF-XS # 7500 was used.
[0045]
An aqueous iodine solution (composition of iodine / potassium iodide / water = 0.05 / 5/100) was used as the staining solution.
[0046]
The measurement of the degree of polarization was calculated by measuring the light transmittance in the polarizing plate at five points using a spectrophotometer after drying the stretched film in accordance with Japan Electronic Machinery Industry Standard (EIJL) LD-201-1983.
[0047]
Washing after dyeing was performed with pure water at 25 ° C. containing 1% of boric acid (HBO 3 ).
[0048]
Wet stretching was carried out in 30 ° C. pure water containing 1% boric acid (HBO 3 ) at a feed rate of 3 m / min, and the roll speed on the winding side was increased according to the stretch ratio.
[0049]
Using the air-stretching apparatus shown in FIG. 1 for the vinylon film, the humidity control and stretching atmosphere conditions are 80 ° C. and 93% relative humidity, and the feed rate is 1 m / min, the take-up speed is 6 m / min, and 6.0 times. Stretched. Then, it was dyed and washed with pure water. Then, after drying for 5 minutes with 50 degreeC warm air, the optical characteristic was implemented about the stretched film.
[0050]
The stretched film had a light transmittance of 42.2%, a degree of polarization of 99.9%, and a light transmittance of 0.04%.
<Example 1>
The 6-fold stretched film obtained in the reference example was dyed again, washed with pure water, then wet-stretched 1.7 times again, and then dried with hot air at 50 ° C. for 5 minutes. Regarding the physical property values of the obtained redrawn film, the light transmittance was 43.1%, the degree of polarization was 99.9%, and the in-plane variation of the light transmittance was 0.21%.
<Example 2>
In the reference example, the humidity was adjusted and the internal temperature of the stretching apparatus was maintained at 70 ° C. and 95% relative humidity, the film was stretched at a take-up speed of 3 m / min (stretching ratio 3 times), and further wet-stretched 2.5 times. Regarding the physical property values of the obtained redrawn film, the light transmittance was 43.3%, the degree of polarization was 99.9%, and the in-plane variation of the light transmittance was 0.40%.
[0051]
【The invention's effect】
Because it is a PVA film manufacturing technology that draws out the advantages of both air-stretching and wet-stretching, neck-in phenomenon can be suppressed during uniaxial stretching. There is an effect that the uniformity is excellent.
[0052]
Since wet stretching is used in combination, the stretching ratio can be increased, and the polarization performance (molecular orientation) can be sufficiently enhanced. In addition, there is no concern that the film breaks as in the case of the dry stretching method, and the effect of enabling stable production is achieved.
[0053]
Furthermore, since the neck-in phenomenon can be suppressed in the stretching in the air, a polarizing film having a high degree of contrast and excellent uniformity in the molecular orientation state in the width direction of the film can be obtained.
[Brief description of the drawings]
FIG. 1 shows an outline of an apparatus for producing a PVA polarizing film according to the present invention.
FIG. 2 is a flowchart showing an overall process including the present invention.
FIG. 3 is an explanatory diagram of a PVA polarizing film in-air stretcher according to the present invention.
[Explanation of symbols]
20 In-air stretching process 21 Unwinder 22 Humidity control device 23 Clean unit 25 Low speed side stretching roller 26 Heating roller 27 High speed side stretching roller 28 Laminating roller 29 Guide roller 30 In-air stretching bath (stretching zone)
31 Different film supply roll 32 Winder 34 Entrance seal box 35 Exit seal box 36 Steaming device 37 Ceiling heating condensation prevention device 38 Wall heating condensation prevention device 42 Swelling process 44 Dyeing process 46 Washing / fixing process 48 Wet stretching process 52 2nd washing process 54 Drying process 62 Laminating process 64 Adhesive layer sticking affirmation 66 Finishing process

Claims (5)

ポリビニールアルコール樹脂よりなる偏光フィルム基材をヨウ素染色される前に1軸延伸する延伸工程と、膨潤処理する工程と、膨潤処理された偏光フィルム基材をヨウ素染色する工程と、ヨウ素染色された偏光フィルム基材を1軸延伸する延伸工程と、延伸工程を経た偏光フィルム基材にヨウ素染色剤を定着させる色剤定着工程と、色剤定着工程を経た偏光フィルム基材を水洗する水洗工程と、水洗工程を経た偏光フィルム基材を乾燥せしめる乾燥工程と、を含むポリビニールアルコール樹脂よりなる液晶セル用偏光フィルムの製造において、
延伸工程としてフィルム表面には全く結露がない状態を保って、未飽和蒸気下で予備加熱して乾燥し、継いで偏光フィルム基材を蒸気浴槽において飽和蒸気に曝し、直ちに延伸することを特徴とする偏光フィルムの製造方法。
A polarizing film substrate made of a polyvinyl alcohol resin is stretched uniaxially before being dyed with iodine, a step of swelling treatment, a step of dyeing the swollen polarizing film substrate with iodine, and iodine dyed A stretching step for uniaxially stretching the polarizing film substrate, a colorant fixing step for fixing an iodine dye to the polarizing film substrate that has undergone the stretching step, and a water washing step for washing the polarizing film substrate that has undergone the coloring agent fixing step with water In the production of a polarizing film for a liquid crystal cell comprising a polyvinyl alcohol resin, including a drying step of drying a polarizing film substrate that has undergone a washing step,
While maintaining the state without completely condensing the film surface as a stretching step, characterized in that to Drying preheated under unsaturated vapor, it succeeded in exposing the polarizing film substrate to saturated steam in the steam bath, immediately stretched A method for producing a polarizing film.
請求項1に記載の偏光フィルムの製造において、水洗工程に硼酸水溶液を使用して水洗処理を施すことを特徴とする偏光フィルムの製造方法。  2. The method for producing a polarizing film according to claim 1, wherein the water washing process is performed using a boric acid aqueous solution in the water washing step. 請求項1に記載の偏光フィルムの製造において、水洗工程に沃化カリ水溶液を使用して水洗処理を施すことを特徴とする偏光フィルムの製造方法。  The method for producing a polarizing film according to claim 1, wherein a washing process is performed using a potassium iodide aqueous solution in the washing step. ポリビニールアルコール樹脂よりなる偏光フィルム基材をヨウ素染色する前に1軸延伸する延伸手段と、膨潤処理する手段と、膨潤処理された偏光フィルム基材をヨウ素染色する染色手段と、ヨウ素染色された偏光フィルム基材を1軸延伸する延伸手段と、延伸工程を経た偏光フィルム基材にヨウ素染色剤を定着させる色剤定着手段と、色剤定着工程を経た偏光フィルム基材を水洗する水洗手段と、水洗工程を経た偏光フィルム基材を乾燥せしめる乾燥手段と、を含むポリビニールアルコール樹脂よりなる偏光フィルムの製造手段において、
気中において実施される延伸手段が、偏光フィルム基材と接する全ての手段に亘り、その表面に全く結露がない状態を保つことができる水蒸気温度よりも少なくとも0.5℃高温度に維持し得る加熱手段を備え、
偏光フィルム基材を未飽和蒸気下で予備加熱して乾燥する手段と、
偏光フィルム基材を蒸気浴槽に導く手段と、
偏光フィルム基材を未飽和蒸気に曝し、直ちに延伸し得る手段を備えたことを特徴とする偏光フィルムの製造装置。
A polarizing film substrate made of a polyvinyl alcohol resin is uniaxially stretched before being dyed with iodine, a means for swelling treatment, a dyeing means for dyeing the swollen polarizing film substrate with iodine, and iodine dyed Stretching means for uniaxially stretching the polarizing film substrate, colorant fixing means for fixing the iodine dyeing agent to the polarizing film substrate that has undergone the stretching process, and water washing means for washing the polarizing film substrate that has undergone the colorant fixing process with water In the means for producing a polarizing film comprising a polyvinyl alcohol resin, including a drying means for drying the polarizing film substrate that has undergone the water washing step,
The stretching means carried out in the air can be maintained at a temperature at least 0.5 ° C. higher than the water vapor temperature that can maintain a state in which no condensation occurs on the surface of all the means in contact with the polarizing film substrate. Heating means,
Means you Drying preheated polarizing film substrate under non-saturated vapor,
Means for guiding the polarizing film substrate to the steam bath;
Apparatus for producing a polarizing film characterized in that a polarizing film substrate subjected to the unsaturated vapor, comprising a means capable of immediately stretch.
請求項4に記載の偏光フィルムの製造装置が、少なくとも1段の気中延伸が可能であって、その延伸倍率は1:2〜8の範囲及び延伸フィルムを湿式又は水系溶媒中再延伸するときの延伸比率は1:1.5〜5.0程度であり、しかも気中延伸温度は60〜120℃の範囲において所定の温度に維持でき、常圧に保持できる気中延伸手段を備えてなる液晶セル用偏光フィルムの製造装置。The apparatus for producing a polarizing film according to claim 4 is capable of at least one step of stretching in the air, the stretching ratio is in the range of 1: 2 to 8, and the stretched film is re-stretched in a wet or aqueous solvent. The stretching ratio is about 1: 1.5 to 5.0, and the air stretching temperature can be maintained at a predetermined temperature in the range of 60 to 120 ° C., and includes an air stretching means that can be maintained at normal pressure. An apparatus for manufacturing a polarizing film for a liquid crystal cell.
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