JPS647575B2 - - Google Patents

Info

Publication number
JPS647575B2
JPS647575B2 JP9784481A JP9784481A JPS647575B2 JP S647575 B2 JPS647575 B2 JP S647575B2 JP 9784481 A JP9784481 A JP 9784481A JP 9784481 A JP9784481 A JP 9784481A JP S647575 B2 JPS647575 B2 JP S647575B2
Authority
JP
Japan
Prior art keywords
film
polyvinyl alcohol
rolling
polarizing
moisture content
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
Application number
JP9784481A
Other languages
Japanese (ja)
Other versions
JPS57212025A (en
Inventor
Nobuo Fukushima
Haruo Hayashida
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP9784481A priority Critical patent/JPS57212025A/en
Publication of JPS57212025A publication Critical patent/JPS57212025A/en
Publication of JPS647575B2 publication Critical patent/JPS647575B2/ja
Granted legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2329/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal, or ketal radical; Hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Derivatives of such polymer
    • C08J2329/02Homopolymers or copolymers of unsaturated alcohols
    • C08J2329/04Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (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]

本発明はポリビニルアルコールまたはその誘導
体からなるフイルムの配向方法に関するものであ
る。本発明方法によつて得られる配向フイルムは
偏光フイルムの製造に有用である。 偏光フイルムは液晶表示装置をはじめ、各種光
学機器、写真用フイルター、サングラス、ビルの
窓など種々の分野で使用されており、一般にポリ
ビニルアルコール系のフイルムに偏光性をもつヨ
ウ素や染料を吸着させ、さらにそのフイルムを数
倍に延伸して作られている。 一般にポリビニルアルコールフイルムの延伸は
湿式法にて行なわれているが、水分によつて分子
間の水素結合が切断され、分子の運動性が増すた
めフイルムの含水率が延伸性に大きな影響を与え
るために、安定加工は容易ではなく、延伸ムラも
生じやすい。 ポリビニルアルコールの二次転移点は含水率の
増加と共に低下し、特に含水率5%付近から急激
に低下することから、5%以上の含水率の下に延
伸が行なわれており、5%以下では延伸困難とさ
れている。 なお、ここで言う含水率とは絶乾状態のPVA
重量に対する水分重量の割合で定義されるもので
ある。 本発明の第1の目的はポリビニルアルコールま
たはその誘導体からなるフイルムを高倍率で、ム
ラなく、安定して配向させる方法を提供すること
にある。 本発明者等は、この目的のために鋭意検討を重
ねた結果、該フイルムの含水率が8%以下であ
り、該フイルムに少くとも50Kg/cm2以上の後方張
力を付与し、20℃以上130℃以下の温度範囲にあ
る対をなす加圧ロールにより少くとも100Kg/cm
以上の線圧にて圧延することにより高倍率で、ム
ラなく配向したフイルムを極めて安定して連続的
に生産できることを見い出し本発明に至つたもの
である。 すなわち、本発明の特徴の1つは乾式法にて配
向できる点にあり、そのため含水工程やそれに伴
つた乾燥工程を必要としないことにある。さらに
他の特徴としては、高倍率でしかも品質的に殆ん
どムラがない均質な配向フイルムを極めて安定し
て連続的に生産できることにある。ここで、高倍
率と言うのは、少くとも2倍以上のことである。 本発明で用いられるポリビニルアルコールまた
はその誘導体としては、ポリビニルアルコール、
ポリビニルホルマールおよびポリビニルアセター
ルなどが用いられる他、それらをエチレン、プロ
ピレン等のオレフインやクロトン酸、アクリル
酸、メタクリル酸、マレイン酸などの不飽和カル
ボン酸あるいはこれらのアルキルエステル、アク
リルアミド等で変性したものも用いることができ
る。 また、上記の他に可塑剤等を配合しても良い。
圧延を行なうに際しては含水率は8%以下である
ことが必要であり、8%を超えると圧延時に加圧
ロールへの粘着が発生するため適当でない。逆に
含水率が8%以下であれば、従来の延伸では困難
とされている含水率5%以下の領域での配向も何
ら支障なく、容易に行なうことができる。また、
加圧ロールの入側で少なくとも50Kg/cm2以上の後
方張力を付与しなければならない。ここで後方張
力とは繰出張力とも呼ばれ、フイルムの進行方向
に対し、逆向きに作用する力のことであり、50
Kg/cm2より低ければ加圧ロールに於ける中立点
(最高圧力点)がロール入側に移行してくいこみ
不良が発生しやすくなり安定加工が難しくなる。 従つて後方張力は50Kg/cm2以上付与することが
必要である。 次に圧延温度に関しては加圧ロールを20℃以上
130℃以下の広範な温度範囲で任意に設定するこ
とができる。 該温度域より温度が低ければ所望の圧延倍率を
得るために多数の加圧ロール群を要することや、
ロール間の加圧に非常に大きな力を必要とし、装
置上問題が生ずると共に、設備的にも高価なもの
となり圧延の条件として不適切である。 また、逆に該温度域より、温度が高ければ該フ
イルムが加圧ロールに粘着すると共に良好な配向
効果をもたらすことが不可能となる。 さらに加圧ロールが該フイルムにかける線圧は
100Kg/cm以上にすることが必要であり、100Kg/
cmより低ければ十分配向させることができない。 なお、圧延に際しては加圧ロールとフイルム間
のマサツ係数を下げるために、圧下点に適当な液
状潤滑液を使用しても良いし、予め、該フイルム
を赤外加熱、遠赤外加熱、高周波加熱、熱風加
熱、スチーム加熱、バス加熱等の加熱方式により
予熱しても良いが、いずれも必要条件ではない。 以上の如くして得られるポリビニルアルコール
またはその誘導体からなる圧延フイルムは、偏光
フイルムとして極めて優れた特性を有しているも
のである。 すなわち、従来、偏光フイルムとしては主にポ
リビニルアルコールの延伸フイルム等が使用され
ているが、前述の如く、ポリビニルアルコールの
延伸は湿式法にて行なわれており、水分によつて
分子間の水素結合が切断され、分子の運動性が増
すことから、フイルムの含水率が延伸性に大きな
影響を与えるために、安定加工は容易ではなく、
延伸ムラも生じやすい欠点がある。 従つて、そうしたフイルムから作成される偏光
フイルムも、当然のことながら品質にムラがあ
り、十分とは言い難い。 しかしながら、本発明によるポリビニルアルコ
ールまたはその誘導体からなる圧延フイルムは、
圧延による配向ムラは殆んどなく、均質なフイル
ムであるため、偏光フイルムにした場合でも極め
て良好な品質特性を有する。 なお、偏光性を付与するためには、該フイルム
にヨウ素や二色性染料等で染着する必要がある
が、本発明では染着剤は特に限定しない。 また、染着は圧延前、圧延時、圧延後のいずれ
で行なつても良い。 ここで言う偏光フイルムの品質とはフイルム外
観の他、主として、光学的性質(単体透過率、直
交透過率、偏光度など)をさす。 なお、単体透過率τMは光が1枚の偏光フイルム
を透過する前の光束F1と透過した後の光束F2
の比によつて定義される。(……τM=F2/F1)直
交透過率τ1は光が吸光軸を直交位に組合せた2枚
の偏光フイルムを通過する前の光束F1と透過後
の光束F3との比によつて定義される。(……τ1
F3/F1) また、偏光度Vは、偏光光束Fをタテ、ヨコの
2方向の振動分が等量の光速Fu(自然光の成分)
とタテまたはヨコのいずれか一方向の振動分の光
速Fp(直線偏光の成分)に分離した時のFとFpと
の比によつて定義される。(……V=Fp/F) 一般に偏光フイルムとして要求される、これら
の光学的性質の値としては 単体透過率……43±2.5% 直交透過率……7%以下 偏光度……85%以上 とされており、本発明による偏光フイルムはこれ
らの要求値を十分満足することができる。 以下、実施例により、本発明を具体的に示す
が、これらにより、本発明は何んら限定されるも
のではない。 実施例 1 厚さ75μのポリビニルアルコールフイルム(ク
ラレビニロン フイルム7500)を直径260φ、面
長700mmの一対の加圧ロールにより3種類の条件
にて圧延し、外観良好な圧延フイルムを連続的に
安定して得ることができた。結果を表1に示す。 なお、用いたフイルムの含水率は2.5%であつ
た。 比較例 1 実施例1と同じ原反を、同じ装置を用いて特許
請求範囲外の3種類の条件にて圧延したところ、
フイルム外観、圧延倍率(2倍以上)加工安定性
のいずれかに問題を生じた。 結果を表1に示す。 比較例 2 実施例1と同じ原反を湿潤状態で、引取速度差
を有するロール群で3種類の条件にて延伸し、比
較的外観良好なフイルムも得られたが、安定した
連続加工は困難であつた。 その際の含水率および結果を表2に示す。 比較例 3 実施例1と同じ原反を引取速度差を有するロー
ル群で3種類の条件にて延伸したが、ロールとフ
イルム間で滑りが発生し、フイルム表面にキズが
発生すると共に折ジワの発生が認められ、条件に
よつてはフイルムの破断が認められた。 結果を表2に示す。 実施例 2 実施例1で得られた圧延フイルムをスミライト
スプラブルーFBGLを5gとノニオン 界面活
性剤0.5gを水1に溶解した染液で35℃にて染
着後、無水硫酸ナトリウム5g、ホウ酸20g、ノ
ニオン 界面活性剤0.1gを水1に溶解した溶
液で洗浄し、70℃で20分間乾燥し、600mの波長
にて単体透過率、直交透過率、偏光度を測定し
た。結果は表1に示す。 比較例 4 比較例2で得られた延伸フイルムのうち、外観
良好なフイルムについて実施例2と同じ方法にて
染着、洗浄、乾燥を行ない、同じく600mμの波
長にて単体透過率、直交透過率、偏光度を測定し
た。 結果は表2に示す。
The present invention relates to a method for orienting a film made of polyvinyl alcohol or its derivatives. The oriented film obtained by the method of the present invention is useful for producing polarizing films. Polarizing films are used in a variety of fields, including liquid crystal display devices, various optical devices, photographic filters, sunglasses, and building windows.Generally, polarizing films are made by adsorbing polarizing iodine and dyes onto polyvinyl alcohol-based films. The film is then stretched several times. Polyvinyl alcohol films are generally stretched using a wet method, but moisture breaks the hydrogen bonds between molecules and increases the mobility of molecules, so the moisture content of the film has a large effect on stretchability. Moreover, stable processing is not easy and uneven stretching tends to occur. The secondary transition point of polyvinyl alcohol decreases as the moisture content increases, and in particular it decreases rapidly from around 5% moisture content, so stretching is carried out at moisture contents of 5% or higher, and below 5%. It is considered difficult to stretch. Note that the moisture content referred to here refers to absolute dry PVA.
It is defined as the ratio of water weight to weight. A first object of the present invention is to provide a method for stably orienting a film made of polyvinyl alcohol or a derivative thereof at high magnification, evenly, and stably. As a result of intensive studies for this purpose, the present inventors have determined that the moisture content of the film is 8% or less, that the film is given a rear tension of at least 50 kg/cm 2 or more, and that At least 100Kg/cm by paired pressure rolls in a temperature range below 130℃
The inventors have discovered that by rolling at the above line pressure, it is possible to continuously produce an evenly oriented film at a high magnification in an extremely stable manner, leading to the present invention. That is, one of the features of the present invention is that orientation can be performed by a dry method, and therefore, there is no need for a hydrous process or a drying process accompanying it. Another feature is that it is possible to continuously produce a homogeneous oriented film with high magnification and almost no unevenness in quality in an extremely stable manner. Here, high magnification means at least twice or more. Polyvinyl alcohol or its derivatives used in the present invention include polyvinyl alcohol,
In addition to polyvinyl formal and polyvinyl acetal, they are also modified with olefins such as ethylene and propylene, unsaturated carboxylic acids such as crotonic acid, acrylic acid, methacrylic acid, and maleic acid, or their alkyl esters, acrylamide, etc. Can be used. Further, in addition to the above, a plasticizer or the like may be added.
When rolling, the moisture content must be 8% or less; if it exceeds 8%, it is not suitable because it will cause sticking to the pressure roll during rolling. On the other hand, if the water content is 8% or less, orientation in a water content range of 5% or less, which is considered difficult with conventional stretching, can be easily performed without any problem. Also,
A rear tension of at least 50 kg/cm 2 must be applied on the entry side of the pressure roll. Here, the backward tension is also called the extending force, and is a force that acts in the opposite direction to the film's traveling direction.
If it is lower than Kg/cm 2 , the neutral point (highest pressure point) of the pressure roll will shift to the roll entry side, making it more likely that defects will occur and stable machining will become difficult. Therefore, it is necessary to apply a rear tension of 50 kg/cm 2 or more. Next, regarding the rolling temperature, set the pressure roll to 20℃ or higher.
It can be set arbitrarily within a wide temperature range of 130℃ or less. If the temperature is lower than this temperature range, a large number of pressure roll groups are required to obtain the desired rolling ratio,
A very large force is required to apply pressure between the rolls, which causes problems with the equipment and also makes the equipment expensive, making it inappropriate as a rolling condition. On the other hand, if the temperature is higher than this temperature range, the film will stick to the pressure roll and it will be impossible to produce a good orientation effect. Furthermore, the linear pressure applied to the film by the pressure roll is
It is necessary to make it more than 100Kg/cm.
If it is lower than cm, sufficient orientation cannot be achieved. In addition, during rolling, in order to reduce the stiffness coefficient between the pressure roll and the film, an appropriate liquid lubricant may be used at the rolling point, or the film may be heated in advance by infrared heating, far infrared heating, or high frequency heating. Preheating may be performed using a heating method such as heating, hot air heating, steam heating, bath heating, etc., but none of them is a necessary condition. The rolled film made of polyvinyl alcohol or its derivatives obtained as described above has extremely excellent properties as a polarizing film. That is, conventionally, stretched films of polyvinyl alcohol have been mainly used as polarizing films, but as mentioned above, stretching of polyvinyl alcohol is carried out by a wet method, and hydrogen bonds between molecules are formed by moisture. Stable processing is not easy because the moisture content of the film has a large effect on stretchability, as the film is cut and molecular mobility increases.
It has the disadvantage that stretching unevenness tends to occur. Therefore, the quality of polarizing films made from such films is naturally uneven and cannot be said to be sufficient. However, the rolled film made of polyvinyl alcohol or its derivatives according to the present invention
Since the film is homogeneous with almost no unevenness in orientation due to rolling, it has extremely good quality characteristics even when made into a polarizing film. In order to impart polarizing properties, it is necessary to dye the film with iodine, a dichroic dye, etc., but the dyeing agent is not particularly limited in the present invention. Further, dyeing may be carried out before rolling, during rolling, or after rolling. The quality of the polarizing film referred to here mainly refers to the optical properties (single transmittance, orthogonal transmittance, degree of polarization, etc.) in addition to the film appearance. Note that the single transmittance τ M is defined by the ratio of the light flux F 1 before the light passes through one polarizing film to the light flux F 2 after the light passes through it. (...τ M = F 2 / F 1 ) The orthogonal transmittance τ 1 is the difference between the luminous flux F 1 before light passes through two polarizing films whose absorption axes are orthogonally combined and the luminous flux F 3 after passing through. defined by the ratio. (...τ 1 =
F 3 /F 1 ) Also, the degree of polarization V is the speed of light Fu (natural light component) when the vibrations of the polarized light flux F in two directions, vertical and horizontal, are equal.
It is defined by the ratio of F and Fp when the speed of light is separated into Fp (linearly polarized component) of vibration in one direction, either vertical or horizontal. (...V=Fp/F) The values of these optical properties generally required for a polarizing film are: Single transmittance...43±2.5% Orthogonal transmittance...7% or less Polarization degree...85% or more The polarizing film according to the present invention can fully satisfy these required values. EXAMPLES Hereinafter, the present invention will be specifically illustrated with reference to Examples, but the present invention is not limited to these in any way. Example 1 A polyvinyl alcohol film (Kuraray Vinylon Film 7500) with a thickness of 75μ was rolled using a pair of pressure rolls with a diameter of 260φ and a surface length of 700mm under three types of conditions, and a rolled film with a good appearance was continuously stabilized. I was able to get it. The results are shown in Table 1. The moisture content of the film used was 2.5%. Comparative Example 1 The same raw material as in Example 1 was rolled using the same equipment under three types of conditions outside the scope of the claims.
Problems occurred in either the film appearance or the processing stability at rolling magnification (2 times or more). The results are shown in Table 1. Comparative Example 2 The same raw material as in Example 1 was stretched in a wet state under three conditions using roll groups with different take-up speeds, and a film with a relatively good appearance was obtained, but stable continuous processing was difficult. It was hot. Table 2 shows the moisture content and results at that time. Comparative Example 3 The same original fabric as in Example 1 was stretched under three conditions using rolls with different take-up speeds, but slipping occurred between the rolls and the film, causing scratches on the film surface and wrinkles. This was observed, and under some conditions, film breakage was observed. The results are shown in Table 2. Example 2 The rolled film obtained in Example 1 was dyed at 35°C with a dye solution prepared by dissolving 5 g of Sumilite Sprablue FBGL and 0.5 g of a nonionic surfactant in 1 part of water, and then dyed with 5 g of anhydrous sodium sulfate and boric acid. 20 g of nonionic surfactant was washed with a solution of 0.1 g of nonionic surfactant dissolved in 1 part of water, dried at 70°C for 20 minutes, and the single transmittance, cross transmittance, and degree of polarization were measured at a wavelength of 600 m. The results are shown in Table 1. Comparative Example 4 Among the stretched films obtained in Comparative Example 2, a film with good appearance was dyed, washed, and dried in the same manner as in Example 2, and the single transmittance and cross transmittance were also measured at a wavelength of 600 mμ. , the degree of polarization was measured. The results are shown in Table 2.

【表】【table】

【表】 実施例 3 実施例1と同じ原反、同じ圧延ロールを用い
て、含水率2.5%、温度105℃、線圧350Kg/cm、
後方張力250Kg/cm2の条件で圧延を施し、延伸倍
率4.0倍の延伸ムラのない外観良好な圧延フイル
ムを連続的に安定して得ることができた。 この圧延フイルムを緊張状態に保つたまま、ヨ
ウ素10g、ヨウ化カリウム150g、水3300gから
なる20℃の液に約60秒間浸漬した。さらに、ホウ
酸150g、水2000gからなる65℃の液に約300秒間
浸漬したのち、20℃の水で1分間水洗を行ない偏
光膜を得た。この偏光膜400〜700mμの可視光線
の波長域における平均の単体透過率は43.3%、偏
光度は97.2%であり、かつフイルム外観も良好で
あつた。
[Table] Example 3 Using the same original fabric and the same rolling roll as in Example 1, the moisture content was 2.5%, the temperature was 105°C, the linear pressure was 350 kg/cm,
Rolling was carried out under the conditions of a rear tension of 250 Kg/cm 2 , and a rolled film with a stretching ratio of 4.0 times, no stretching unevenness, and a good appearance could be continuously and stably obtained. The rolled film was immersed in a 20° C. solution containing 10 g of iodine, 150 g of potassium iodide, and 3,300 g of water for about 60 seconds while keeping it under tension. Further, the film was immersed in a solution of 150 g of boric acid and 2000 g of water at 65°C for about 300 seconds, and then washed with water at 20°C for 1 minute to obtain a polarizing film. This polarizing film had an average single transmittance of 43.3% in the visible light wavelength range of 400 to 700 mμ, a polarization degree of 97.2%, and a good film appearance.

Claims (1)

【特許請求の範囲】[Claims] 1 ポリビニルアルコールまたはその誘導体から
なるフイルムを配向せしめるに際して、該フイル
ムの含水率を5%以下とし、該フイルムに少くと
も50Kg/cm2以上の後方張力を付与し、20℃以上、
130℃以下の温度範囲にある対をなす加圧ロール
により、少くとも100Kg/cm以上の線圧にて圧延
することを特徴とするポリビニルアルコールまた
はその誘導体からなるフイルムの配向方法。
1. When orienting a film made of polyvinyl alcohol or its derivatives, the moisture content of the film is set to 5% or less, a backward tension of at least 50 kg/cm 2 or more is applied to the film, and the film is heated at 20°C or higher,
1. A method for orienting a film made of polyvinyl alcohol or a derivative thereof, which comprises rolling at a linear pressure of at least 100 kg/cm or more using a pair of pressure rolls in a temperature range of 130° C. or less.
JP9784481A 1981-06-23 1981-06-23 Orientation of polyvinyl alcohol base film Granted JPS57212025A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9784481A JPS57212025A (en) 1981-06-23 1981-06-23 Orientation of polyvinyl alcohol base film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9784481A JPS57212025A (en) 1981-06-23 1981-06-23 Orientation of polyvinyl alcohol base film

Publications (2)

Publication Number Publication Date
JPS57212025A JPS57212025A (en) 1982-12-27
JPS647575B2 true JPS647575B2 (en) 1989-02-09

Family

ID=14203024

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9784481A Granted JPS57212025A (en) 1981-06-23 1981-06-23 Orientation of polyvinyl alcohol base film

Country Status (1)

Country Link
JP (1) JPS57212025A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6010207A (en) * 1983-06-30 1985-01-19 Mitsui Toatsu Chem Inc Production of polarizing film
JP2731813B2 (en) * 1987-04-17 1998-03-25 住友化学工業株式会社 Manufacturing method of oriented film
JP2632242B2 (en) * 1990-11-30 1997-07-23 富士写真フイルム株式会社 Method for producing retardation film
JPH08240715A (en) * 1995-03-03 1996-09-17 Sumitomo Chem Co Ltd Polarizing film manufacturing method
JP4405075B2 (en) 2000-12-19 2010-01-27 日東電工株式会社 Polarizing film, manufacturing method thereof, and polarizing plate using the same
JP4149201B2 (en) * 2002-06-12 2008-09-10 株式会社クラレ Manufacturing method of polarizing film

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53129265A (en) * 1977-04-18 1978-11-11 Osaka Gouseihin Kk Method for making polyvinyl alchol sheets

Also Published As

Publication number Publication date
JPS57212025A (en) 1982-12-27

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