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JP3283564B2 - Method for producing polyvinyl alcohol-based film - Google Patents
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JP3283564B2 - Method for producing polyvinyl alcohol-based film - Google Patents

Method for producing polyvinyl alcohol-based film

Info

Publication number
JP3283564B2
JP3283564B2 JP4654192A JP4654192A JP3283564B2 JP 3283564 B2 JP3283564 B2 JP 3283564B2 JP 4654192 A JP4654192 A JP 4654192A JP 4654192 A JP4654192 A JP 4654192A JP 3283564 B2 JP3283564 B2 JP 3283564B2
Authority
JP
Japan
Prior art keywords
film
temperature
drying
heat treatment
weight
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP4654192A
Other languages
Japanese (ja)
Other versions
JPH05245858A (en
Inventor
信雄 田中
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
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Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP4654192A priority Critical patent/JP3283564B2/en
Publication of JPH05245858A publication Critical patent/JPH05245858A/en
Application granted granted Critical
Publication of JP3283564B2 publication Critical patent/JP3283564B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Polarising Elements (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Moulding By Coating Moulds (AREA)
  • Shaping By String And By Release Of Stress In Plastics And The Like (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は偏光膜の作成に用いる
リビニルアルコール系フィルムの製造方法に関するもの
である。さらに詳しくいえば、本発明は、偏光性能と耐
久性に優れた偏光膜の作成に用いるポリビニルアルコー
ル系フィルムを効率よく製造する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyvinyl alcohol film used for forming a polarizing film . More specifically, the present invention relates to a method for efficiently producing a polyvinyl alcohol-based film used for producing a polarizing film having excellent polarization performance and durability.

【0002】[0002]

【従来の技術】従来、ポリビニルアルコールフィルム
は、通常金属加熱ロールを使用し、実質上完全乾燥する
ことにより作成されている。このような方法で得られる
フィルムは、全厚みにわたって均質な物性を有するため
に、多くの用途において、形状安定性に優れたポリビニ
ルアルコールフィルムとして利用されており、そしてそ
の用途の一つとして偏光膜が知られている。該偏光膜は
光の透過および遮蔽機能を有し、光のスイッチング機能
をもつ液晶とともに液晶ディスプレイ(LCD)の基本
的な構成要素として用いられている。このLCDは、近
年、初期の頃の電卓や時計などの小型機器から、ラップ
トップ型パーソナルコンピューター,ワードプロセッサ
ー,液晶カラープロジェクター,車載用ナビゲーション
システム,液晶テレビなどの高品位でかつ高信頼性の要
求される機器へと拡大してきている。このような状況に
おいて、該偏光膜に対しても従来のものより一段と優れ
た偏光特性と耐久性とを併せもつ偏光膜が要望されてい
る。したがって、このような要望に応えるために、これ
まで、例えば特殊の染料を用いる方法、有機溶剤溶液を
ゲル製膜して基材のポリビニルアルコールフィルムを製
造する方法などが提案されている。しかしながら、これ
らの方法においては、染料作製が困難であったり、有機
溶剤を使用する場合は安全面や設備保全面で費用が増大
するのを免れないなどの欠点があった。
2. Description of the Related Art Conventionally, a polyvinyl alcohol film is usually prepared by using a metal heating roll and drying it substantially completely. The film obtained by such a method is used as a polyvinyl alcohol film having excellent shape stability in many applications because of having uniform physical properties over the entire thickness, and one of the applications is a polarizing film. It has been known. The polarizing film has a function of transmitting and blocking light, and is used as a basic component of a liquid crystal display (LCD) together with a liquid crystal having a function of switching light. In recent years, LCDs have been required from small devices such as calculators and watches in the early days to high quality and high reliability such as laptop personal computers, word processors, liquid crystal color projectors, in-vehicle navigation systems, and liquid crystal televisions. Equipment. Under these circumstances, there is a demand for a polarizing film having both more excellent polarization characteristics and durability than conventional polarizing films. Therefore, in order to meet such demands, for example, a method using a special dye, a method for producing a polyvinyl alcohol film as a base material by forming a gel from an organic solvent solution, and the like have been proposed. However, these methods have drawbacks such as difficulty in producing dyes, and the use of an organic solvent inevitably increases costs in terms of safety and equipment maintenance.

【0003】[0003]

【発明が解決しようとする課題】本発明は、このような
事情のもとで、優れた偏光特性と耐久性とを併せもつ偏
光膜の作成に用いるポリビニルアルコール系フィルムを
効率よく製造する方法を提供することを目的としてなさ
れたものである。
SUMMARY OF THE INVENTION Under the above circumstances, the present invention provides a method for efficiently producing a polyvinyl alcohol-based film used for producing a polarizing film having excellent polarization characteristics and durability. It was made for the purpose of providing.

【0004】[0004]

【課題を解決するための手段】本発明者は前記目的を達
成するために鋭意研究を重ねた結果、1個の回転体によ
り構成される片面乾燥タイプの乾燥装置とそれと直結す
る熱処理装置とを有する製膜機を使用して、ポリビニル
アルコール系樹脂水溶液膜に一定の水分率になるまで乾
燥処理を施し、次により高温で熱処理を施すことによ
り、熱水切断温度と重量膨潤度との積がある値以上のポ
リビニルアルコール系フィルムが得られ、このものは偏
光特性及び耐久性に優れる偏光膜の作成に適しているこ
とを見出した。本発明はかかる知見に基づいて完成した
ものである。
Means for Solving the Problems The present inventor has conducted intensive studies to achieve the above object, and as a result, has found a single-sided drying type drying apparatus composed of one rotating body and a heat treatment apparatus directly connected thereto. Using a film forming machine having a film, a polyvinyl alcohol-based resin aqueous solution film is subjected to a drying treatment until a constant moisture content is obtained, and then subjected to a heat treatment at a higher temperature, whereby the product of the hot water cutting temperature and the weight swelling degree is obtained. A polyvinyl alcohol-based film having a certain value or more was obtained, and it was found that this film was suitable for producing a polarizing film having excellent polarization characteristics and durability. The present invention has been completed based on such findings.

【0005】すなわち、本発明は、1個の回転体により
構成される片面乾燥タイプの乾燥装置とそれと直結する
熱処理装置とを有する製膜機を用いてポリビニルアルコ
ール系樹脂水溶液膜からポリビニルアルコール系フィル
ムを製造するに際し、フィルムの水分率が2〜15重量
%に到達した時点でフィルムを乾燥工程から熱処理工程
へ移すこと、及び乾燥温度より高い温度で熱処理するこ
とを特徴とする熱水切断温度T(℃)と重量膨潤度W
(%)との積T×W(℃・%)が13000以上である
偏光膜の作成に用いるポリビニルアルコール系フィルム
の製造方法を提供するものである。
That is, the present invention uses a film forming machine having a one-sided drying type drying device composed of one rotating body and a heat treatment device directly connected to the drying device to convert a polyvinyl alcohol-based resin aqueous solution film into a polyvinyl alcohol-based film. Wherein the film is transferred from a drying step to a heat treatment step when the moisture content of the film reaches 2 to 15% by weight, and is subjected to a heat treatment at a temperature higher than the drying temperature. (° C) and weight swelling degree W
(%) And the product T × W (° C.%) are 13,000 or more
An object of the present invention is to provide a method for producing a polyvinyl alcohol-based film used for producing a polarizing film .

【0006】本発明の方法で得られるポリビニルアルコ
ール系フィルム(以下、ポリビニルアルコールをPV
A、ポリビニルアルコール系フィルムをPVA系フィル
ムと略称する)は、熱水切断温度T(℃)と重量膨潤度
W(%)との積T×W(℃・%)が13000以上、好
ましくは14000以上、より好ましくは15000以
上であることが必要である。このT×Wの値が1300
0未満では偏光膜にした際に高偏光特性又は高耐久性あ
るいはその両方の特性を十分に発現できないおそれがあ
る。ここでいう重量膨潤度W(%)の測定法は次の通り
である。すなわち、試料フィルム3gを約3mm幅に裁
断し、30℃の温水に15分間浸漬後、300rpmで
5分間遠心脱水した後の試料重量を(W1)、それを1
05℃で16時間乾燥した後の試料重量を(W2)とす
ると、重量膨潤度W(%)は次式により求められる。重
量膨潤度W(%)=(W1)/(W2)×100 ・・
・ (I)また、熱水切断温度T(℃)の測定法は次の
通りである。すなわち、幅5mm,長さ15cmの試料
に0.5g/10μmの重りを取り付けて40℃の温度の
水中に吊り下げ、その後水温を3℃/分の速度で昇温
し、試料が切断する際の温水温度を、熱水切断温度T
(℃)として求める。
The polyvinyl alcohol-based film obtained by the method of the present invention (hereinafter, polyvinyl alcohol is referred to as PV
A, a polyvinyl alcohol-based film is abbreviated as a PVA-based film), the product T × W (° C.%) of the hot water cutting temperature T (° C.) and the degree of weight swelling W (%) is 13,000 or more, preferably 14000. It is necessary to be at least 15,000 . The value of this T × W 1300
If it is less than 0, high polarization characteristics and / or high durability or both characteristics may not be sufficiently exhibited when a polarizing film is formed. The method of measuring the degree of weight swelling W (%) is as follows. That is, 3 g of a sample film was cut into a width of about 3 mm, immersed in warm water of 30 ° C. for 15 minutes, and centrifuged and dehydrated at 300 rpm for 5 minutes to obtain a sample weight of (W1).
Assuming that the sample weight after drying at 05 ° C. for 16 hours is (W2), the weight swelling degree W (%) is obtained by the following equation. Weight swelling degree W (%) = (W1) / (W2) × 100
(I) The method of measuring the hot water cutting temperature T (° C.) is as follows. That is, a sample having a width of 5 mm and a length of 15 cm is attached with a weight of 0.5 g / 10 μm and suspended in water at a temperature of 40 ° C., and then the water temperature is raised at a rate of 3 ° C./min. Hot water temperature, hot water cutting temperature T
(° C).

【0007】本発明の方法においては、前記PVA系フ
ィルムは、1個の回転体により構成される片面乾燥タイ
プの乾燥装置とそれと直結する熱処理装置を有する製膜
機を使用してPVA系樹脂水溶液膜から、PVA系フィ
ルムを製膜するに際し、フィルムの水分率が2〜15重
量%、好ましくは3〜10重量%に到達した時点でフィ
ルムを乾燥工程から熱処理工程に移すこと、及び乾燥温
度より高い温度で熱処理することにより得られる。本発
明においては、乾燥装置として1個の回転体により構成
される片面乾燥タイプのものが用いられ。具体的には回
転加熱ドラムや回転加熱ベルト(あるいはロール)など
が使用可能であり、これらの乾燥装置では、PVA系樹
脂水溶液膜の乾燥は、ドラム側(ドラム面)では行われ
ず、ドラムと反対のフリー面でのみ行われる。該回転加
熱ドラムあるいは回転加熱ドラムの周囲を熱風チャンバ
ーで覆い、熱風加熱を併用すると、乾燥効率が向上し有
利である。本発明には、乾燥装置に直結した熱処理装置
が必要であり、この熱処理装置には加熱ロール又は熱風
炉などが使用できる。なお、上述の乾燥工程における乾
燥温度は、特に制限はないが、通常は60〜140℃、
好ましくは70〜120℃である。また、熱処理工程に
おける熱処理についても、乾燥温度より高い温度であれ
ば特に制限はなく、様々な状況に応じて適宜選定すれば
よいが、通常は80〜140℃、好ましくは100〜1
30℃である。
[0007] In the method of the present invention, the PVA-based film is prepared by using a PVA-based resin aqueous solution by using a film-forming machine having a single-side drying type drying apparatus composed of one rotating body and a heat treatment apparatus directly connected thereto. When a PVA-based film is formed from the film, the film is transferred from the drying step to the heat treatment step when the water content of the film reaches 2 to 15% by weight, preferably 3 to 10% by weight, and Obtained by heat treatment at a high temperature. In the present invention, a single-sided drying type constituted by one rotating body is used as a drying device. Specifically, a rotary heating drum, a rotary heating belt (or a roll), or the like can be used. In these drying devices, drying of the PVA-based resin aqueous solution film is not performed on the drum side (drum surface), but is performed on the opposite side of the drum. It only takes place on the free side. When the rotary heating drum or the periphery of the rotary heating drum is covered with a hot air chamber and hot air heating is used in combination, the drying efficiency is advantageously improved. The present invention requires a heat treatment device directly connected to a drying device, and a heat roll or a hot blast stove can be used for this heat treatment device. The drying temperature in the above-mentioned drying step is not particularly limited, but is usually 60 to 140 ° C,
Preferably it is 70-120 degreeC. Also, the heat treatment in the heat treatment step is not particularly limited as long as it is higher than the drying temperature, and may be appropriately selected depending on various situations, but is usually from 80 to 140 ° C., preferably from 100 to 1 ° C.
30 ° C.

【0008】次に本発明の方法により、PVA系フィル
ムを製造する好適な態様の一例について説明すると、ま
ず流延キャスト法や押出キャストなどの公知の方法によ
って、PVA系樹脂水溶液を乾燥装置の乾燥面、例えば
金属回転加熱ドラム表面にキャストしてPVA系樹脂水
溶液膜を形成する。このPVA系樹脂水溶液膜は直ちに
乾燥過程に入り、該水溶液膜のフリー面側(ドラムと反
対面側)の乾燥が先行する。乾燥が進行し、フィルム全
体の平均水分率が2〜15重量%、好ましくは3〜10
重量%に達した時点で熱処理工程に移す。この熱処理工
程におけるPVA系フィルム温度は、前記乾燥工程にお
けるPVA系フィルム温度より高くなるように熱処理時
の加熱温度を設定する必要がある。熱処理工程を経ると
PVA系フィルムは通常絶乾に達するので、その後調湿
処理を施すことにより、所望の水分が付与されたPVA
系フィルムが得られる。
Next, an example of a preferred embodiment for producing a PVA-based film by the method of the present invention will be described. First, a PVA-based resin aqueous solution is dried in a drying apparatus by a known method such as a casting method or an extrusion casting method. A PVA-based resin aqueous solution film is formed by casting on a surface, for example, a metal rotary heating drum surface. The PVA-based resin aqueous solution film immediately enters a drying process, and drying of the free surface side (the opposite side to the drum) of the aqueous solution film is preceded. Drying proceeds, and the average moisture content of the entire film is 2 to 15% by weight, preferably 3 to 10%.
When the weight% is reached, the process proceeds to a heat treatment step. It is necessary to set the heating temperature during the heat treatment so that the PVA-based film temperature in the heat treatment step is higher than the PVA-based film temperature in the drying step. After the heat treatment step, the PVA-based film usually reaches an absolutely dry state.
A base film is obtained.

【0009】前記乾燥工程から熱処理工程へ移る際のP
VA系フィルムの水分率が2重量%未満や15重量%を
超える場合は、いずれも高偏光性及び高耐久性を有する
ものが得られず、本発明の目的が達成されない。このよ
うにして得られたPVA系フィルムが高偏光特性を発現
する理由は次のように推定される。すなわち、該PVA
系フィルムが乾燥工程から熱処理工程へ移る際のフィル
ム全体の(全厚み平均)の水分率は2〜15重量%であ
るが、厚み方向の位置で異なっており、フリー面側は乾
燥が進んで水分がほとんどなく、ドラム面側に多くの水
分が偏在している。このようなフィルムが熱処理工程へ
入ると、水分率の高いドラム面側の結晶化は進むが、水
分をほとんどもたないフリー面側の結晶化は進みが少な
い。その結果、該フィルムの結晶性が低く、したがって
重量膨潤度の高い片面(フリー面側)と、結晶性が高く
て熱水切断温度の高い他方の片面(ドラム面側)とを有
することになり、この結果、PVA系フィルムの重量膨
潤度と熱水切断温度との積が高くなったと推定される。
また、このフィルムから偏光膜を作成する際には、片面
の優れた染色性,延伸時配向性と、他方の片面の優れた
耐熱水性すなわち優れた高温延伸性とが相俟って、高偏
光特性及び高耐久性が発現されるものと推定される。
[0009] P when transferring from the drying step to the heat treatment step
When the moisture content of the VA-based film is less than 2% by weight or more than 15% by weight, a film having high polarization and high durability cannot be obtained, and the object of the present invention cannot be achieved. The reason why the thus obtained PVA-based film exhibits high polarization characteristics is presumed as follows. That is, the PVA
When the system film moves from the drying step to the heat treatment step, the moisture content of the entire film (average of the total thickness) is 2 to 15% by weight, but differs in the position in the thickness direction. There is almost no water, and much water is unevenly distributed on the drum surface side. When such a film enters the heat treatment step, crystallization on the drum surface side having a high moisture content proceeds, but crystallization on the free surface side having little moisture hardly progresses. As a result, the film has one surface (free surface side) having low crystallinity and therefore a high degree of weight swelling, and the other surface (drum surface side) having high crystallinity and high hot water cutting temperature. As a result, it is estimated that the product of the degree of weight swelling of the PVA-based film and the hot water cutting temperature was increased.
In addition, when a polarizing film is prepared from this film, high dyeing properties and orientation during stretching are combined with excellent hot water resistance, that is, excellent high temperature stretchability on one side, resulting in high polarization. It is estimated that characteristics and high durability are exhibited.

【0010】このようにして得られたPVA系フィル
用いて偏光膜を製造するには、公知の方法、例えばP
VA系フィルムに染色,延伸,ホウ酸化合物処理等を施
したのち、乾燥して偏光膜を作成する方法などを利用す
ることができる。染色は一軸延伸の前,延伸中,延伸後
のいずれにおいて施してもよいし、また染料としては、
例えばヨウ素−ヨウ化カリウム、あるいは二色性染料な
どを使用することができる。延伸の温水中で行ってもよ
いし、吸水後のフィルムを空気中で行ってもよく、延伸
温度は、通常30℃以上、好ましくは40℃以上、より
好ましくは50℃以上が有利である。さらに、ホウ酸化
合物処理においては、ホウ酸化合物浴中にヨウ素化合物
を混合してもよい。このようにして得られた偏光膜に
は、通常その両外面に各種の支持体、例えば三酢酸セル
ロースがラミネートされる。
[0010] The PVA-based fill-time obtained in this way
In order to manufacture a polarizing film by using a known method, for example, P
A method in which a VA-based film is dyed, stretched, treated with a boric acid compound, and then dried to form a polarizing film can be used. Dyeing may be performed before, during or after uniaxial stretching, and as a dye,
For example, iodine-potassium iodide or a dichroic dye can be used. The stretching may be performed in warm water or the film after water absorption may be performed in the air. The stretching temperature is usually 30 ° C. or higher, preferably 40 ° C. or higher, more preferably 50 ° C. or higher. Further, in the boric acid compound treatment, an iodine compound may be mixed in the boric acid compound bath. The polarizing film thus obtained is usually laminated with various supports, for example, cellulose triacetate, on both outer surfaces thereof.

【0011】本発明において使用できる原料のPVA系
樹脂としては、酢酸ビニルを重合して得られるポリ酢酸
ビニルをけん化して製造される、いわゆる通常のPVA
のほか、不飽和カルボン酸又はその誘導体、不飽和スル
ホン酸又はその誘導体、炭素数2〜30のα−オレフィ
ンなどで約15モル%未満共重合された変性ポリビニル
アルコール、あるいはポリビニルホルマール,ポリビニ
ルアセトアセタール,ポリビニルブチラールなどのポリ
ビニルアセタールや、エチレン単位含量が20モル%以
上のエチレン−ビニルアルコール共重合体等を挙げるこ
とができる。
The raw material PVA-based resin usable in the present invention is a so-called ordinary PVA produced by saponifying polyvinyl acetate obtained by polymerizing vinyl acetate.
A modified polyvinyl alcohol copolymerized with an unsaturated carboxylic acid or a derivative thereof, an unsaturated sulfonic acid or a derivative thereof, an α-olefin having 2 to 30 carbon atoms, and the like, in an amount of less than about 15 mol%, or polyvinyl formal or polyvinyl acetoacetal And polyvinyl acetal such as polyvinyl butyral, and an ethylene-vinyl alcohol copolymer having an ethylene unit content of 20 mol% or more.

【0012】本発明におけるPVA系樹脂としては、重
合度が500以上、好ましくは2400以上、より好ま
しくは4000以上のものが偏光特性及び耐久性に優れ
ているので好適である。また、該PVA系樹脂のけん化
度は90モル%以上、好ましくは95モル%以上、より
好ましくは98モル%以上であるのが、耐久性に優れ望
ましい。本発明におけるPVA系フィルムを作成する際
の溶媒としては、水,有機溶剤あるいはこれらの混合物
のいずれも使用することができるが、本発明は水単独溶
媒系で高偏光特性及び高耐久性のPVA系フィルムが得
られる点に特徴があり、当然ながら安全面,経済面で優
れる水溶媒の使用が有利である。本発明のPVA系フィ
ルムの厚みは、通常5〜150μm、好ましくは30〜
100μmの範囲で選ばれる。また、該PVA系フィル
ムには、グリセリンなどの各種のポリオール系可塑剤
や、ノニオン性,アニオン性,カチオン性の界面活性剤
などの添加成分を、所望に応じて適宜添加してもよい。
As the PVA-based resin in the present invention, those having a degree of polymerization of 500 or more, preferably 2400 or more, more preferably 4000 or more are suitable because they have excellent polarization characteristics and durability. In addition, the degree of saponification of the PVA-based resin is preferably at least 90 mol%, more preferably at least 95 mol%, more preferably at least 98 mol%, because it is excellent in durability and desirable. As the solvent for preparing the PVA-based film in the present invention, any of water, an organic solvent and a mixture thereof can be used. However, the present invention relates to a water-only solvent-based PVA having high polarization characteristics and high durability. A characteristic feature is that a base film can be obtained. Naturally, it is advantageous to use a water solvent which is excellent in safety and economy. The thickness of the PVA-based film of the present invention is usually 5 to 150 μm, preferably 30 to 150 μm.
It is selected in the range of 100 μm. Further, to the PVA-based film, various polyol-based plasticizers such as glycerin, and additional components such as nonionic, anionic and cationic surfactants may be appropriately added as required.

【0013】[0013]

【実施例】次に実施例により本発明をさらに詳細に説明
するが、本発明はこれらの例によってなんら限定される
ものではない。なお、実施例及び比較例において、フィ
ルムの水分率はフィルムサンプルの乾燥前重量を(G
1)、50℃,16時間真空乾燥後の重量を(G2)と
すると、式 フィルムの水分率(%)=(G1−G2)/G1×100 ・・(II) により求められる。また、偏光膜製造工程における共通
の製造条件などは次の通りである。すなわち、染色浴の
染料濃度はヨウ素/ヨウ化カリウム重量比を1/10に
固定し、ヨウ素濃度を1〜20g/リットルの範囲内で
適宜選択して、単体透過率43%近辺の偏光膜を採取し
た。ホウ酸浴のホウ酸濃度は4重量%とし、延伸浴にも
ホウ酸を4重量%濃度になるように添加した。乾燥は5
0℃の熱風で行った。
Next, the present invention will be described in more detail by way of examples, which should not be construed as limiting the present invention. In Examples and Comparative Examples, the moisture content of the film was determined by the weight (G) of the film sample before drying.
1) Assuming that the weight after vacuum drying at 50 ° C. for 16 hours is (G2), the moisture content (%) of the film can be obtained by the following equation: (G1−G2) / G1 × 100 (II) Common manufacturing conditions in the polarizing film manufacturing process are as follows. That is, the dye concentration of the dyeing bath is fixed at a weight ratio of iodine / potassium iodide of 1/10, and the iodine concentration is appropriately selected within a range of 1 to 20 g / liter to obtain a polarizing film having a single transmittance of about 43%. Collected. The concentration of boric acid in the boric acid bath was 4% by weight, and boric acid was added to the stretching bath so as to have a concentration of 4% by weight. Drying is 5
The test was performed with hot air at 0 ° C.

【0014】本発明では偏光性能を表現するのに二色性
比を用いた。この二色性比は偏光膜の光線透過率(単体
透過率)Ts(%)と偏光度P(%)から式 二色性比=log(Ts/100-Ts ×P/10000)/log (Ts/100+ Ts ×P/10000) ・・・(III) で求められる。また、耐久性の評価は、偏光膜の両面に
PVA系接着剤を用いて厚さ80μmの三酢酸セルロー
スを貼り合わせて得た偏光板を、温度60℃,相対湿度
(RH)90%の雰囲気下に200時間放置した後の単
体透過率及び偏光度を測定して行った。
In the present invention, the dichroic ratio is used to express the polarization performance. The dichroic ratio is calculated from the light transmittance (single transmittance) Ts (%) of the polarizing film and the degree of polarization P (%) using the formula: dichroic ratio = log (Ts / 100-Ts × P / 10000) / log ( Ts / 100 + Ts × P / 10000) ··· Determined in (III). The durability was evaluated by bonding a polarizing plate obtained by bonding a 80 μm-thick cellulose triacetate to both surfaces of a polarizing film using a PVA-based adhesive at a temperature of 60 ° C. and a relative humidity (RH) of 90%. The measurement was performed by measuring the single transmittance and the degree of polarization after being left for 200 hours.

【0015】実施例1 押出機,ダイ,周囲が熱風炉で覆われた単一の回転加熱
金属ドラムからなる乾燥装置及び熱風炉式の熱処理装置
からなる製膜機を用いて、回転加熱金属ドラム温度を7
5℃,熱風温度を75℃,熱処理装置の熱風温度を12
0℃に設定した。重合度1700,けん化度99.9モル
%のPVA41重量部,水54重量部およびグリセリン
5重量部からなるペレットを回転加熱金属ドラムにキャ
ストし乾燥,熱処理を連続して行い、膜厚75μmのP
VAフィルムを作成した。得られたフィルムの重量膨潤
度は210%、熱水切断温度は65℃、したがって重量
膨潤度と熱水切断温度との積は13650であった。ま
た、乾燥装置と熱処理装置の中間で採取したフィルムの
水分率は4.2重量%であった。
EXAMPLE 1 A rotary heating metal drum was formed by using a film forming machine comprising a single rotary heating metal drum covered with an extruder, a die and a hot stove and a hot stove type heat treatment apparatus. Temperature 7
5 ° C, hot air temperature 75 ° C, heat air temperature of heat treatment equipment 12
It was set to 0 ° C. A pellet composed of 41 parts by weight of PVA having a degree of polymerization of 1700 and a saponification degree of 99.9 mol%, 54 parts by weight of water and 5 parts by weight of glycerin was cast on a rotary heating metal drum, dried and heat-treated continuously, and a 75 μm-thick P
A VA film was made. The obtained film had a weight swelling degree of 210% and a hot water cutting temperature of 65 ° C., and therefore, the product of the weight swelling degree and the hot water cutting temperature was 13650. The moisture content of the film collected between the drying device and the heat treatment device was 4.2% by weight.

【0016】応用例1 上記実施例1で得られたフィルムに、染色,延伸,ホウ
酸処理及び乾燥を順次施して偏光膜を作成した。延伸可
能な上限の水温(以下、延伸時の上限水温と略記する)
35℃、延伸可能な上限の延伸倍率(以下、上限延伸倍
率と略記する)5.3倍の条件にて一軸延伸した。得られ
た偏光膜の単体透過率は43.3%、偏光度は98.8%、
二色性比は35.1で優れた偏光性能を有していた。
Application Example 1 The film obtained in Example 1 was sequentially subjected to dyeing, stretching, boric acid treatment and drying to form a polarizing film. Upper limit water temperature at which stretching is possible (hereinafter abbreviated as upper limit water temperature during stretching)
The film was uniaxially stretched under the conditions of 35 ° C. and 5.3 times the maximum stretch ratio at which stretching was possible (hereinafter abbreviated as the upper limit stretch ratio). The obtained polarizing film has a single transmittance of 43.3%, a degree of polarization of 98.8%,
The dichroic ratio was 35.1, indicating excellent polarization performance.

【0017】実施例2 実施例1と同じ製膜機を用いて、回転加熱金属ドラム温
度を90℃、熱風温度を90℃、熱処理装置の熱風温度
を120℃に設定した。重合度4000のけん化度99.
6モル%のPVA35重量部,水60重量部およびグリ
セリン5重量部からなるペレットを回転加熱金属ドラム
上にキャストし、乾燥,熱処理を連続して行い、膜厚7
5μmのPVAフィルムを作成した。得られたフィルム
の重量膨潤度は215%、熱水切断温度は70℃、した
がって重量膨潤度と熱水切断温度との積は15050で
あった。また、乾燥装置と熱処理装置の中間で採取した
フィルムの水分率は8.5重量%であった。
Example 2 Using the same film forming machine as in Example 1, the temperature of the rotary heating metal drum was set to 90 ° C., the temperature of hot air was set to 90 ° C., and the temperature of hot air of the heat treatment apparatus was set to 120 ° C. Degree of saponification with polymerization degree of 4000
A pellet composed of 35 parts by weight of PVA of 6 mol%, 60 parts by weight of water and 5 parts by weight of glycerin was cast on a rotary heating metal drum, and dried and heat-treated continuously, and a film thickness of 7% was obtained.
A 5 μm PVA film was made. The weight swelling degree of the obtained film was 215%, the hot water cutting temperature was 70 ° C., and the product of the weight swelling degree and the hot water cutting temperature was 15050. The moisture content of the film collected between the drying device and the heat treatment device was 8.5% by weight.

【0018】応用例2 上記実施例2で得られたフィルムに、染色,延伸,ホウ
酸処理及び乾燥を順次施して偏光膜を作成した。延伸時
の上限水温50℃、上限延伸倍率5.0倍の条件にて一軸
延伸した。得られた偏光膜の単体透過率は43.2%、偏
光度は99.7%、二色性比は45.0で優れた偏光性能を
有していた。この偏光膜の耐久性テスト後の単体透過率
は47.3%、偏光度は93.6%、二色性比は39.7で優
れた耐久性を示した。
Application Example 2 The film obtained in Example 2 was sequentially subjected to dyeing, stretching, boric acid treatment and drying to form a polarizing film. Uniaxial stretching was performed under the conditions of an upper limit water temperature of 50 ° C. and an upper limit stretch ratio of 5.0 at the time of stretching. The polarizing film obtained had a single transmittance of 43.2%, a degree of polarization of 99.7%, and a dichroic ratio of 45.0, showing excellent polarizing performance. After the durability test, the polarizing film had a single transmittance of 47.3%, a degree of polarization of 93.6%, and a dichroic ratio of 39.7, indicating excellent durability.

【0019】比較例1 実施例1と同じ製膜機を用いて、回転加熱金属ドラム温
度を70℃、熱風温度を70℃、熱処理装置の熱風温度
を150℃に設定した。実施例1と同じペレットを回転
加熱金属ドラムにキャストし、乾燥,熱処理を連続して
行い、膜厚75μmのPVAフィルムを作成した。得ら
れたフィルムの重量膨潤度は163%、熱水切断温度は
74℃、したがって重量膨潤度と熱水切断温度との積は
12062であった。また、乾燥装置と熱処理装置の中
間で採取したフィルムの水分率は4.4重量%であった。
次に、このフィルムに染色,延伸,ホウ酸処理及び乾燥
を順次施して偏光膜を作成した。延伸時の上限水温50
℃、上限延伸倍率4.4倍の条件にて一軸延伸した。得ら
れた偏光膜の単体透過率は42.6%、偏光度は94.6
%、二色性比は20.1で偏光性能の劣るものであった。
Comparative Example 1 Using the same film forming machine as in Example 1, the temperature of the rotary heating metal drum was set at 70 ° C., the temperature of hot air was set at 70 ° C., and the temperature of hot air of the heat treatment apparatus was set at 150 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and drying and heat treatment were continuously performed to form a PVA film having a thickness of 75 μm. The degree of weight swelling of the obtained film was 163%, the hot water cutting temperature was 74 ° C., and therefore, the product of the weight swelling degree and the hot water cutting temperature was 12062. The moisture content of the film collected between the drying device and the heat treatment device was 4.4% by weight.
Next, the film was sequentially dyed, stretched, treated with boric acid, and dried to form a polarizing film. Maximum water temperature during stretching 50
The film was uniaxially stretched under the conditions of ° C and an upper limit stretching ratio of 4.4 times. The obtained polarizing film had a single transmittance of 42.6% and a degree of polarization of 94.6.
%, The dichroic ratio was 20.1, indicating poor polarization performance.

【0020】比較例2 実施例1と同じ製膜機を用いて、回転加熱金属ドラム温
度を85℃、熱風温度を85℃、熱処理装置の熱風温度
を120℃に設定した。実施例1と同じペレットを回転
加熱金属ドラムにキャストし、乾燥,熱処理を連続して
行い、膜厚75μmのPVAフィルムを作成した。得ら
れたフィルムの重量膨潤度は205%、熱水切断温度は
62℃、したがって重量膨潤度と熱水切断温度との積は
12710であった。また、乾燥装置と熱処理装置の中
間で採取したフィルムの水分率は0.8重量%であった。
次に、このフィルムに染色,延伸,ホウ酸処理及び乾燥
を順次施して偏光膜を作成した。延伸時の上限水温30
℃、上限延伸倍率4.5倍の条件にて一軸延伸した。得ら
れた偏光膜の単体透過率は43.0%、偏光度は92.6
%、二色性比は18.3で偏光性能の劣るものであった。
Comparative Example 2 Using the same film forming machine as in Example 1, the temperature of the rotary heating metal drum was set to 85 ° C., the temperature of hot air was set to 85 ° C., and the temperature of hot air of the heat treatment apparatus was set to 120 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and drying and heat treatment were continuously performed to form a PVA film having a thickness of 75 μm. The weight swelling degree of the obtained film was 205%, and the hot water cutting temperature was 62 ° C. Therefore, the product of the weight swelling degree and the hot water cutting temperature was 12,710. The moisture content of the film collected between the drying device and the heat treatment device was 0.8% by weight.
Next, the film was sequentially dyed, stretched, treated with boric acid, and dried to form a polarizing film. Maximum water temperature during stretching 30
The film was uniaxially stretched at a temperature of 4.5 ° C. and an upper limit of 4.5 times. The obtained polarizing film has a single transmittance of 43.0% and a degree of polarization of 92.6.
%, And the dichroic ratio was 18.3, indicating poor polarization performance.

【0021】比較例3 実施例1と同じ製膜機を用いて、回転加熱金属ドラム温
度を50℃、熱風温度を50℃、熱処理装置の熱風温度
を120℃に設定した。実施例1と同じペレットを回転
加熱金属ドラムにキャストし、乾燥,熱処理を連続して
行い、膜厚75μmのPVAフィルムを作成した。得ら
れたフィルムの重量膨潤度は180%、熱水切断温度は
67℃、したがって重量膨潤度と熱水切断温度との積は
12060であった。また、乾燥装置と熱処理装置の中
間で採取したフィルムの水分率は20.6重量%であっ
た。次に、このフィルムに染色,延伸,ホウ酸処理及び
乾燥を順次施して偏光膜を作成した。延伸時の上限水温
35℃、上限延伸倍率4.5倍の条件にて一軸延伸した。
得られた偏光膜の単体透過率は44.3%、偏光度は93.
8%、二色性比は23.6で偏光性能の劣るものであっ
た。
Comparative Example 3 Using the same film forming machine as in Example 1, the temperature of the rotary heating metal drum was set to 50 ° C., the temperature of hot air was set to 50 ° C., and the temperature of hot air of the heat treatment apparatus was set to 120 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and drying and heat treatment were continuously performed to form a PVA film having a thickness of 75 μm. The weight swelling degree of the obtained film was 180%, the hot water cutting temperature was 67 ° C., and the product of the weight swelling degree and the hot water cutting temperature was 12060. The moisture content of the film collected between the drying device and the heat treatment device was 20.6% by weight. Next, the film was sequentially dyed, stretched, treated with boric acid, and dried to form a polarizing film. The film was uniaxially stretched under the conditions of an upper limit water temperature of 35 ° C. and an upper limit stretch ratio of 4.5 at the time of stretching.
The obtained polarizing film has a single transmittance of 44.3% and a degree of polarization of 93.
The dichroic ratio was 83.6% and the polarization performance was inferior.

【0022】比較例4 実施例1と同じ製膜機を用いて、回転加熱金属ドラム温
度を90℃、熱風温度を90℃に設定し、実施例2と同
じペレット用いてキャストし、乾燥のみを行って膜厚7
5μmの未熱処理PVAフィルムを得た。このフィルム
の水分率は8.5重量%であった。このフィルムロールを
1日間放置後、実施例1と同じ熱処理装置を用いて、熱
処理を行い熱処理ずみPVAフィルムを得た。得られた
フィルムの重量膨潤度は177%、熱水切断温度は71
℃、したがって重量膨潤度と熱水切断温度との積は12
567であった。次に、このフィルムに染色,延伸,ホ
ウ酸処理及び乾燥を順次施して偏光膜を作成した。延伸
時の上限水温50℃、上限延伸倍率4.4倍の条件にて一
軸延伸した。得られた偏光膜の単体透過率は43.6%、
偏光度は94.0%、二色性比は21.7で偏光性能に劣る
ものであった。
Comparative Example 4 Using the same film forming machine as in Example 1, the temperature of the rotary heating metal drum was set to 90 ° C., the temperature of the hot air was set to 90 ° C., and the same pellets as in Example 2 were cast. Go to film thickness 7
A 5 μm unheated PVA film was obtained. The moisture content of this film was 8.5% by weight. After leaving this film roll for one day, it was subjected to heat treatment using the same heat treatment apparatus as in Example 1 to obtain a heat-treated PVA film. The weight swelling degree of the obtained film was 177%, and the hot water cutting temperature was 71%.
° C, thus the product of the degree of weight swelling and the hot water cutting temperature is 12
567. Next, the film was sequentially dyed, stretched, treated with boric acid, and dried to form a polarizing film. Uniaxial stretching was performed under the conditions of an upper limit water temperature of 50 ° C. and an upper limit stretching ratio of 4.4 times during stretching. The single transmittance of the obtained polarizing film is 43.6%,
The degree of polarization was 94.0% and the dichroic ratio was 21.7, which was inferior to the polarization performance.

【0023】[0023]

【発明の効果】本発明の方法によると、偏光特性及び耐
久性に極めて優れる偏光膜の作成に良好なPVA系フィ
ルムが容易に得られる。このPVA系フィルムから得ら
れた偏光膜は、例えばパーソナルコンピューター,ワー
ドプロセッサー,テレビ用など、従来の偏光膜以上の特
性が要求されるLCD分野にも十分適用できる。
According to the method of the present invention, good PVA-based film can be easily obtained in the creation of an extremely excellent polarization film of the polarization property and durability. The polarizing film obtained from the PVA-based film can be sufficiently applied to the LCD field, for example, for a personal computer, a word processor, a television, and the like, which requires more characteristics than conventional polarizing films.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 1個の回転体により構成される片面乾燥
タイプの乾燥装置とそれと直結する熱処理装置とを有す
る製膜機を用いてポリビニルアルコール系樹脂水溶液膜
からポリビニルアルコール系フィルムを製造するに際
し、フィルムの水分率が2〜15重量%に到達した時点
でフィルムを乾燥工程から熱処理工程へ移すこと、及び
乾燥温度より高い温度で熱処理することを特徴とする熱
水切断温度T(℃)と重量膨潤度W(%)との積T×W
(℃・%)が13000以上である、偏光膜の作成に用
いるポリビニルアルコール系フィルムの製造方法。
1. A method for producing a polyvinyl alcohol-based film from a polyvinyl alcohol-based resin aqueous solution film using a film-forming machine having a single-sided drying type drying device constituted by one rotating body and a heat treatment device directly connected thereto. When the water content of the film reaches 2 to 15% by weight, the film is transferred from the drying step to the heat treatment step, and the heat treatment is performed at a temperature higher than the drying temperature. Product T × W with weight swelling degree W (%)
(° C.%) is 13000 or more, for making polarizing film
Method for producing a polyvinyl alcohol film which are.
JP4654192A 1992-03-04 1992-03-04 Method for producing polyvinyl alcohol-based film Expired - Fee Related JP3283564B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4654192A JP3283564B2 (en) 1992-03-04 1992-03-04 Method for producing polyvinyl alcohol-based film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4654192A JP3283564B2 (en) 1992-03-04 1992-03-04 Method for producing polyvinyl alcohol-based film

Publications (2)

Publication Number Publication Date
JPH05245858A JPH05245858A (en) 1993-09-24
JP3283564B2 true JP3283564B2 (en) 2002-05-20

Family

ID=12750160

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4654192A Expired - Fee Related JP3283564B2 (en) 1992-03-04 1992-03-04 Method for producing polyvinyl alcohol-based film

Country Status (1)

Country Link
JP (1) JP3283564B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE328940T1 (en) * 2000-05-01 2006-06-15 Kuraray Co POLYVINYL ALCOHOL FILM AND POLARIZING FILM
JP4646356B2 (en) * 2000-05-12 2011-03-09 株式会社クラレ Production method of polyvinyl alcohol film
TWI230275B (en) * 2000-05-12 2005-04-01 Kuraray Co Polyvinyl alcohol film and polarization film
JP4530522B2 (en) * 2000-11-15 2010-08-25 株式会社クラレ Method for cutting vinyl alcohol polymer film for drawing
JP4764658B2 (en) * 2005-04-28 2011-09-07 日本合成化学工業株式会社 Method for producing polyvinyl alcohol film
JP5628025B2 (en) * 2008-12-18 2014-11-19 株式会社クラレ Polyvinyl alcohol film
JP4904415B2 (en) * 2010-05-14 2012-03-28 株式会社クラレ Method for cutting vinyl alcohol polymer film for drawing
JP6033721B2 (en) * 2012-03-30 2016-11-30 株式会社クラレ Film roll and its package
WO2015076169A1 (en) 2013-11-21 2015-05-28 株式会社クラレ Polyvinyl alcohol film
KR102475406B1 (en) * 2015-08-18 2022-12-07 미쯔비시 케미컬 주식회사 Polyvinyl alcohol-based film and polarizing film made using the same

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