JP2001164000A - Method of producing norbornene based resin film - Google Patents

Method of producing norbornene based resin film

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Publication number
JP2001164000A
JP2001164000A JP35034399A JP35034399A JP2001164000A JP 2001164000 A JP2001164000 A JP 2001164000A JP 35034399 A JP35034399 A JP 35034399A JP 35034399 A JP35034399 A JP 35034399A JP 2001164000 A JP2001164000 A JP 2001164000A
Authority
JP
Japan
Prior art keywords
film
norbornene
based resin
temperature
resin film
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.)
Pending
Application number
JP35034399A
Other languages
Japanese (ja)
Inventor
Tsunatoshi Ishimaru
維敏 石丸
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.)
Sekisui Chemical Co Ltd
Original Assignee
Sekisui 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 Sekisui Chemical Co Ltd filed Critical Sekisui Chemical Co Ltd
Priority to JP35034399A priority Critical patent/JP2001164000A/en
Publication of JP2001164000A publication Critical patent/JP2001164000A/en
Pending legal-status Critical Current

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  • Manufacture Of Macromolecular Shaped Articles (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve the problem of allowing fine ruggedness of a film or streaks of the film which are parallel to the stretching direction to cause phase difference nonuniformity in the film after stretching when a norbornene based resin film produced by solution casting is uniaxially stretched in the lengthwise direction to produce a phase difference film. SOLUTION: The method of producing a norbonene based resin film by solution casting comprises passing the obtained film between a pair of nip rolls whose clearance is set at 95-100% average thickness of the film in a drying oven whose temperature is set in the range of from the initiation temperature of deforming the film to not higher than the initiation temperature of deforming the film plus 100 deg.C at the last stage of the drying step.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は溶液キャスト法によ
るノルボルネン系樹脂フィルムの製造方法に関する。さ
らに詳しくは、反射型液晶表示装置の位相差フィルムと
して好適に使用することが出来る光学用透明ノルボルネ
ン系樹脂フィルムの製造方法に関する。
The present invention relates to a method for producing a norbornene resin film by a solution casting method. More specifically, the present invention relates to a method for producing a transparent optical norbornene resin film that can be suitably used as a retardation film of a reflection type liquid crystal display device.

【0002】[0002]

【従来の技術】近年開発された反射型液晶表示装置にお
いては、これに用いられる液晶の波長分散との兼ね合い
から、波長分散の低い材料による位相差フィルムが求め
られている。
2. Description of the Related Art In a reflection type liquid crystal display device developed in recent years, a retardation film made of a material having a low wavelength dispersion is demanded in consideration of the wavelength dispersion of a liquid crystal used in the device.

【0003】ノルボルネン系樹脂は、ポリカーボネート
やポリサルフォン等のエンジニアリングプラスチックや
トリアセチルセルロースに比べて、応力を加えた際の複
屈折が小さく、また屈折率の波長分散特性が小さいとい
う特徴を有しているため、反射型液晶表示装置に好適な
光学フィルム材料として注目されている。
[0003] Norbornene-based resins are characterized by having a smaller birefringence when stress is applied and a smaller wavelength dispersion characteristic of the refractive index than engineering plastics such as polycarbonate and polysulfone and triacetyl cellulose. Therefore, it is attracting attention as an optical film material suitable for a reflection type liquid crystal display device.

【0004】ノルボルネン系樹脂フィルムは溶液キャス
ト法によって製膜できることが特開平4−361230
号公報に記載されている。
It has been disclosed that a norbornene-based resin film can be formed by a solution casting method.
No., published in Japanese Unexamined Patent Publication No.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、溶液キ
ャスト法により製造したノルボルネン系樹脂フィルムを
縦一軸延伸して位相差フィルムを製造すると、フィルム
の微小な凹凸あるいは延伸方向の平行なスジが延伸後の
フィルムにおいて位相差ムラを引き起こすという問題が
あった。
However, when a retardation film is manufactured by longitudinally and uniaxially stretching a norbornene-based resin film manufactured by a solution casting method, fine unevenness of the film or stripes parallel to the stretching direction are generated after stretching. There was a problem that retardation unevenness was caused in the film.

【0006】本発明者は上述の課題を解決するために鋭
意研究した結果、ノルボルネン系樹脂キャストフィルム
の微小な凹凸あるいは延伸方向の平行なスジが延伸時に
助長され、位相差ムラを引き起こし、この現象は特定条
件下においてニップロール間にキャストフィルムを通す
と見事に解消できることを見出し、本発明を完成するに
至った。
The present inventor has conducted intensive studies to solve the above-mentioned problems. As a result, fine irregularities or streaks parallel to the stretching direction of the norbornene-based resin cast film are promoted at the time of stretching, causing phase difference unevenness. Found that it was possible to solve the problem by passing a cast film between nip rolls under specific conditions, and completed the present invention.

【0007】本発明の目的は、位相差フィルムとして使
用した場合に位相差の局所的な変化を防止することが出
来る光学用透明ノルボルネン系樹脂フィルムの製造方法
を提供することにある。
An object of the present invention is to provide a method for producing a transparent optical norbornene resin film which can prevent a local change in retardation when used as a retardation film.

【0008】[0008]

【課題を解決するための手段】すなわち、本発明は、溶
液キャスト法によるノルボルネン系樹脂フィルムの製造
方法において、乾燥工程の最後に、フィルム変形開始温
度以上であって変形開始温度+100℃以下の温度範囲
に設定された乾燥炉内において、得られたフィルムを平
均フィルム厚の95〜100%にクリアランスが設定さ
れた一対のニップロール間を通すことを特徴とするノル
ボルネン系樹脂フィルムの製造方法を提供するものであ
る。
That is, the present invention relates to a method for producing a norbornene-based resin film by a solution casting method, wherein at the end of the drying step, a temperature not lower than the film deformation start temperature and not higher than the deformation start temperature + 100 ° C. A method for producing a norbornene-based resin film, characterized in that the obtained film is passed between a pair of nip rolls having a clearance set to 95 to 100% of the average film thickness in a drying furnace set in a range. Things.

【0009】[0009]

【発明の実施の形態】以下、本発明の構成について詳述
する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The configuration of the present invention will be described below in detail.

【0010】本発明は、透明ノルボルネン系樹脂位相差
フィルムに発生する位相差ムラを厚み精度を向上させる
ことにより防止するものである。キャストフィルムの厚
み精度は製膜に依存するところが大きいが、これは溶液
の粘度とコーターの相性やあるいは乾燥条件、流延基材
等の様々な条件が絡んでいる。これらの条件を詰めるこ
とで膜厚精度を高めることも可能であるが、本発明では
より簡便に厚み精度を高めて位相差ムラの発生を防止で
きる点で優れている。
[0010] The present invention is to prevent the retardation unevenness occurring in the transparent norbornene resin retardation film by improving the thickness accuracy. The thickness accuracy of the cast film largely depends on the film formation, but this is related to the viscosity of the solution and the compatibility of the coater, or various conditions such as drying conditions and casting base materials. Although it is possible to increase the film thickness accuracy by reducing these conditions, the present invention is excellent in that the thickness accuracy can be more easily increased and the occurrence of phase difference unevenness can be prevented.

【0011】本発明において、ノルボルネン系樹脂フィ
ルムは溶液キャスト法によって製膜され、溶液調整に用
いる溶剤、溶液キャスト法については従来の公知の手段
をそのまま用いることができる。
In the present invention, the norbornene-based resin film is formed by a solution casting method, and the solvent used for adjusting the solution and the solution casting method can be used by a conventionally known means as it is.

【0012】溶液キャスト法において、樹脂溶液に用い
るノルボルネン系樹脂は熱可塑性飽和ノルボルネン系樹
脂であり、例えば、特開平3−14882号公報、特開
平3−122137号公報などに開示されている公知の
樹脂であり、従来公知の熱可塑性飽和ノルボルネン系樹
脂を好適に使用することが出来る。
In the solution casting method, the norbornene-based resin used in the resin solution is a thermoplastic saturated norbornene-based resin, and is, for example, a known one disclosed in JP-A-3-14882 and JP-A-3-122137. It is a resin, and a conventionally known thermoplastic saturated norbornene-based resin can be suitably used.

【0013】熱可塑性飽和ノルボルネン系樹脂を構成す
るモノマーを例示すると、例えば、ノルボルネン、5−
メチル−2−ノルボルネン、5−エチル−2−ノルボル
ネン、5−ブチル−2−ノルボルネン、5−エチリデン
−2−ノルボルネン、5−メトキシカルボニル−2−ノ
ルボルネン、5,5−ジメチル−2−ノルボルネン、5
−シアノ−2−ノルボルネン、5−メチル−5−メトキ
シカルボニル−2−ノルボルネン、5−フェニル−2−
ノルボルネン、5−フェニル−5−メチル−2−ノルボ
ルネン、エチレン−テトラシクロドデセン共重合体、6
−メチル−1,4:5,8−ジメタノ−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
エチル−1,4:5,8−ジメタノ−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
エチル−1,4:5,8−エチリデン−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
クロロ−1,4:5,8−ジメタノ−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
シアノ−1,4:5,8−ジメタノ−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
ピリジル−1,4:5,8−ジメタノ−1,4,4a,
5,6,7,8,8a−オクタヒドロナフタレン、6−
メトキシカルボニル−1,4:5,8−ジメタノ−1,
4,4a,5,6,7,8,8a−オクタヒドロナフタ
レン、1,4−ジメタノ−1,4,4a,4b,5,
8,8a,9a−オクタヒドロフルオレン、5,8−メ
タノ−1,2,3,4,4a,5,8,8a−オクタヒ
ドロ−2.3−シクロペンタジエノナフタレン、4,
9:5,8−ジメタノ−3a,4,4a,5,8,8
a,9,9a−オクタヒドロ−1H−ベンゾインデン、
4,11:5,10:6,9−トリメタノ−3a,4,
4a,5,5a,6,9,9a,10,10a,11,
11a−ドデカヒドロ−1H−シクロペンタアントラセ
ン等が挙げられる。
Examples of monomers constituting the thermoplastic saturated norbornene resin include, for example, norbornene, 5-
Methyl-2-norbornene, 5-ethyl-2-norbornene, 5-butyl-2-norbornene, 5-ethylidene-2-norbornene, 5-methoxycarbonyl-2-norbornene, 5,5-dimethyl-2-norbornene, 5
-Cyano-2-norbornene, 5-methyl-5-methoxycarbonyl-2-norbornene, 5-phenyl-2-
Norbornene, 5-phenyl-5-methyl-2-norbornene, ethylene-tetracyclododecene copolymer, 6
-Methyl-1,4: 5,8-dimethano-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Ethyl-1,4: 5,8-dimethano-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Ethyl-1,4: 5,8-ethylidene-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Chloro-1,4: 5,8-dimethano-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Cyano-1,4: 5,8-dimetano-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Pyridyl-1,4: 5,8-dimetano-1,4,4a,
5,6,7,8,8a-octahydronaphthalene, 6-
Methoxycarbonyl-1,4: 5,8-dimetano-1,
4,4a, 5,6,7,8,8a-octahydronaphthalene, 1,4-dimethano-1,4,4a, 4b, 5
8,8a, 9a-octahydrofluorene, 5,8-methano-1,2,3,4,4a, 5,8,8a-octahydro2.3-cyclopentadienonenaphthalene, 4,
9: 5,8-Dimethano-3a, 4,4a, 5,8,8
a, 9,9a-octahydro-1H-benzoindene,
4,11: 5,10: 6,9-trimethano-3a, 4,4
4a, 5, 5a, 6, 9, 9a, 10, 10a, 11,
11a-dodecahydro-1H-cyclopentaanthracene and the like.

【0014】熱可塑性飽和ノルボルネン系樹脂は、例え
ば、(イ)ノルボルネン系モノマーの開環重合体若しく
は開環共重合体を、必要に応じてマレイン酸付加、シク
ロペンタジエン付加の如き変性を行った後に、水素添加
した樹脂、(ロ)ノルボルネン系モノマーを付加重合さ
せた樹脂、(ハ)ノルボルネン系モノマーとエチレンや
α−オレフィンなどのオレフィン系モノマーと付加重合
させた樹脂、(ニ)ノルボルネン系モノマーとシクロペ
ンテン、シクロオクテン、5,6−ジヒドロジシクロペ
ンタジエンなどの環状オレフィン系モノマーと付加重合
させた樹脂、これらの樹脂の変性物等が挙げられる。
The thermoplastic saturated norbornene-based resin is obtained, for example, by subjecting (a) a ring-opening polymer or a ring-opening copolymer of a norbornene-based monomer to modification such as addition of maleic acid or cyclopentadiene, if necessary. Hydrogenated resin, (b) a resin obtained by addition polymerization of a norbornene-based monomer, (c) a resin obtained by addition polymerization of a norbornene-based monomer and an olefin-based monomer such as ethylene or α-olefin, and (d) a norbornene-based monomer. Resins obtained by addition polymerization with a cyclic olefin monomer such as cyclopentene, cyclooctene, 5,6-dihydrodicyclopentadiene, and modified products of these resins.

【0015】上記重合は、例えば、重合媒体としてI
r、Os、Ruの三塩化物の含水塩、MoCl5、W
l6、ReCl5、(C253Al、(C253Al
/TiCl4、(π−C474Mo/TiCl4、(π
−C474W/TiCl4、(π−C 353Cr/W
Cl6等を用いて、常法により行うことができる。
In the above polymerization, for example, I
r, Os, Ru trichloride hydrate, MoCl5, W
Cl6, ReClFive, (CTwoHFive)ThreeAl, (CTwoHFive)ThreeAl
/ TiClFour, (Π-CFourH7)FourMo / TiClFour, (Π
-CFourH7)FourW / TiClFour, (Π-C ThreeHFive)ThreeCr / W
Cl6And the like, using a conventional method.

【0016】上記熱可塑性飽和ノルボルネン系樹脂とし
ては、日本ゼオン社より商品名「ZEONOR」、「Z
EONEX」、ジェイエスアール社より商品名「ART
ON」、三井石油化学社より商品名「APEL]として
上市されている。
As the above-mentioned thermoplastic saturated norbornene resin, trade names "ZEONOR", "Z
"EONEX", product name "ART" from JSR Corporation
ON ", which is marketed by Mitsui Petrochemical Company as" APEL ".

【0017】熱可塑性飽和ノルボルネン系樹脂の数平均
分子量は、小さくなると耐湿性が低下し透湿度が大きく
なり、大きくなるとフィルム成形性が低下するので、ト
ルエン溶媒によるゲル・パーミュエーション・クロマト
グラフで測定して、2万5千〜10万が好ましく、より
好ましくは3万〜8万である。
When the number average molecular weight of the thermoplastic saturated norbornene resin decreases, the moisture resistance decreases and the moisture permeability increases, and as the number average molecular weight increases, the film formability decreases. Therefore, the gel permeation chromatograph using a toluene solvent is used. When measured, it is preferably 25,000 to 100,000, and more preferably 30,000 to 80,000.

【0018】上記ノルボルネン系樹脂を溶解するための
溶媒としては、沸点が100℃以上好ましくは120℃
以上のものが好ましく、例えば、トルエン、キシレン、
エチルベンゼン、トリメチルベンゼン、クロロベンゼン
等がある。その中でもトルエン、エチルベンゼン、クロ
ルベンゼンが好ましい。樹脂溶液の濃度としては10〜
50重量%が好ましい。
The solvent for dissolving the norbornene resin may have a boiling point of 100 ° C. or higher, preferably 120 ° C.
The above are preferred, for example, toluene, xylene,
There are ethylbenzene, trimethylbenzene, chlorobenzene and the like. Among them, toluene, ethylbenzene and chlorobenzene are preferred. The concentration of the resin solution is 10 ~
50% by weight is preferred.

【0019】溶液キャスト法については特に限定され
ず、ポリカーボネート樹脂フィルムなどの光学フィルム
の製造に用いられる一般的な溶液キャスト方法を用いる
ことができ、具体的にはバーコーター、ロールコータ
ー、ダイコーター、コンマコーターなどを用いて、支持
体としてポリエチレンテレフタレートなどの耐熱材料や
スチールベルト等の平板またはロール上に、樹脂溶液を
流延することができる。
The solution casting method is not particularly limited, and a general solution casting method used for producing an optical film such as a polycarbonate resin film can be used. Specifically, a bar coater, a roll coater, a die coater, Using a comma coater or the like, the resin solution can be cast on a heat-resistant material such as polyethylene terephthalate or a flat plate or a roll such as a steel belt as a support.

【0020】樹脂溶液の流延後の乾燥工程も特に制限は
なく従来公知の方法を用いることが出来るが数段階に分
けて行うことが好ましく、1段階の乾燥としては比較的
低い温度100℃以下の温度で乾燥を行い溶剤の急激な
揮発による発泡が発生しない温度で乾燥を行い、2段階
以降の乾燥において高温化して乾燥を行う。
The drying step after the casting of the resin solution is not particularly limited, and a conventionally known method can be used. However, the drying is preferably performed in several steps, and the drying in one step is performed at a relatively low temperature of 100 ° C. or less. And drying at a temperature at which foaming due to rapid evaporation of the solvent does not occur.

【0021】本発明においては、乾燥の最後の段階にお
いて、乾燥炉内に樹脂フィルムの変形開始温度から変形
開始温度+100℃の乾燥温度となるゾーンを設け、こ
のゾーン内でフィルムの最終厚みの95〜100%にク
リアランスが調整されたニップロール間を通す。本発明
において変形開始温度とはチャック間距離が50mmに
設定された加熱炉付引き張り試験器で10gの一定荷重
をかけ5℃/分で昇温しながら伸びを測定し伸びが1%
を越えた温度である。変形開始温度はフィルムに含まれ
る溶剤の含有量、粘性等によって適宜調整することがで
きる。変形開始温度から100℃を超える高温である場
合、樹脂フィルムは容易に変形してしまい、幅や厚み等
が設定とずれてしまう。また、ニップロールからの剥離
性が悪くなり、フィルムの変形の発生や厚み精度が低下
する場合がある。
In the present invention, in the last stage of the drying, a zone is provided in the drying furnace where the drying temperature is from the deformation start temperature of the resin film to the deformation start temperature + 100 ° C. In this zone, the final thickness of the film is 95%. Pass between nip rolls with clearance adjusted to ~ 100%. In the present invention, the term "deformation start temperature" refers to the elongation measured by elongation at a temperature of 5 ° C./min while applying a constant load of 10 g with a tensile tester equipped with a heating furnace in which the distance between chucks is set to 50 mm.
The temperature exceeds. The deformation start temperature can be appropriately adjusted depending on the content, viscosity, etc. of the solvent contained in the film. When the temperature is higher than the deformation starting temperature and exceeds 100 ° C., the resin film is easily deformed, and the width, thickness, and the like deviate from the settings. In addition, the releasability from the nip roll is deteriorated, which may cause deformation of the film and decrease the thickness accuracy.

【0022】ニップロール表面は樹脂との剥離性が高い
表面処理がなされていることが好ましい。例えば、ハー
ドクロームメッキやタングステンカーバイト処理などが
あるが処理方法は限定されるものではなく、樹脂特性に
適した処理方法を用いればよい。
It is preferable that the surface of the nip roll is subjected to a surface treatment having a high releasability from the resin. For example, there are hard chrome plating and tungsten carbide treatment, but the treatment method is not limited, and a treatment method suitable for resin characteristics may be used.

【0023】ニップロールを設置する乾燥炉の加熱方法
としては、温度の均一性からは熱風加熱方式が好ましい
が、フィルムの変形が容易にできる温度領域での加熱と
なるため、風速、風向は極力フィルムの余計な変形を起
こさないように設定する必要がある。例えばフィルムの
走行方向に平行した風を流すカウンターフロー方式があ
る。あるいは、熱風加熱方式と、遠赤外線加熱または赤
外線加熱方式を併用した方法を用いることができる。
As a method of heating the drying furnace in which the nip roll is installed, a hot air heating method is preferable from the viewpoint of temperature uniformity. However, since the heating is performed in a temperature range where the film can be easily deformed, the wind speed and the wind direction are minimized. It is necessary to set so as not to cause unnecessary deformation. For example, there is a counter flow method in which a wind parallel to the running direction of the film is passed. Alternatively, a method using both a hot air heating method and a far infrared heating or infrared heating method can be used.

【0024】上記の条件下でニップロールを通したフィ
ルムは厚み精度が高く、延伸処理することにより、位相
差ムラのない位相差フィルムとして好適に使用される。
The film passed through the nip roll under the above conditions has a high thickness accuracy and can be suitably used as a retardation film having no retardation unevenness by stretching.

【0025】[0025]

【実施例】次ぎに本発明を実施例を挙げてさらに具体的
に説明するが、本発明は以下の実施例のみに限定される
ものではない。
EXAMPLES Next, the present invention will be described more specifically with reference to examples, but the present invention is not limited to the following examples.

【0026】「実施例1」日本ゼオン(株)社製ノルボ
ルネン系樹脂「ZEONEX」を用いて、樹脂濃度が4
0重量%となるトルエン溶液を調整した。これをコンマ
コーターを用いてPETフィルム上に乾燥厚みが80μ
mとなるように流延した。これを100℃、120℃、
140℃の3つのゾーンからなる乾燥ゾーンを通し乾燥
した。このときライン速度は1m/分、各ゾーンの滞留
時間は5分である。ZEONEXフィルムを25mm幅
に切り出し、加熱炉付の引き張り試験器でチャック間距
離を50mmにしてサンプルをセットし、10gの一定
荷重をかけ、5℃/分で昇温しながら伸びが1%を越え
る温度(変形開始温度)を測定したところ変形開始温度
は62℃であった。厚みは79μmであった。次にPE
Tフィルムから剥離したZEONEXフィルムを、12
0℃、150℃の乾燥ゾーンを1m/分のライン速度で
通し乾燥を行った。それぞれの乾燥ゾーンの滞留時間は
25分である。150℃の乾燥ゾーンにはクリアランス
を74μmに調整した一対のニップロールを設けた。7
5.4μm厚の光学用透明ノルボルネン系樹脂フィルム
を得た。
Example 1 Using a norbornene resin "ZEONEX" manufactured by Zeon Corporation and having a resin concentration of 4
A 0% by weight toluene solution was prepared. This was dried on a PET film using a comma coater to a dry thickness of 80μ.
m. 100 ° C, 120 ° C,
It was dried through a drying zone consisting of three zones at 140 ° C. At this time, the line speed is 1 m / min, and the residence time in each zone is 5 minutes. A ZEONEX film was cut into a width of 25 mm, a sample was set with a tensile tester equipped with a heating furnace with a distance between chucks of 50 mm, a constant load of 10 g was applied, and the temperature was raised at 5 ° C./min. When the temperature exceeding the temperature (deformation start temperature) was measured, the deformation start temperature was 62 ° C. The thickness was 79 μm. Next, PE
ZEONEX film peeled from T film
Drying was performed by passing through a drying zone of 0 ° C. and 150 ° C. at a line speed of 1 m / min. The residence time in each drying zone is 25 minutes. The drying zone at 150 ° C. was provided with a pair of nip rolls whose clearance was adjusted to 74 μm. 7
An optical transparent norbornene resin film having a thickness of 5.4 μm was obtained.

【0027】「実施例2」JSR(株)社製ノルボルネ
ン系樹脂「ARTON」を用いて、樹脂濃度が30重量
%となるトルエン溶液を調整した。これをコンマコータ
ーを用いてPETフィルム上に乾燥厚みが80μmとな
るように流延した。これを100℃、120℃、140
℃の3つのゾーンからなる乾燥ゾーンを通し乾燥した。
このときライン速度は1m/分、各ゾーンの滞留時間は
5分である。ARTONフィルムを25mm幅に切り出
し、加熱炉付の引き張り試験器でチャック間距離を50
mmにしてサンプルをセットし、10gの一定荷重をか
け、5℃/分で昇温しながら伸びが1%を越える温度
(変形開始温度)を測定したところ変形開始温度は65
℃であった。厚みは80μmであった。次にPETフィ
ルムから剥離したARTONフィルムを、125℃、1
50℃を1m/分のライン速度で通し乾燥を行った。そ
れぞれの乾燥ゾーンの滞留時間は25分である。150
℃の乾燥ゾーンにはクリアランスを76μmに調整した
一対のニップロールを設けた。76.1μm厚の光学用
透明ノルボルネン系樹脂フィルムを得た。
Example 2 A toluene solution having a resin concentration of 30% by weight was prepared using a norbornene resin "ARTON" manufactured by JSR Corporation. This was cast on a PET film using a comma coater so that the dry thickness was 80 μm. 100 ° C, 120 ° C, 140
It dried through the drying zone which consists of three zones of ° C.
At this time, the line speed is 1 m / min, and the residence time in each zone is 5 minutes. The ARTON film is cut into 25 mm width, and the distance between the chucks is set to 50 using a tensile tester equipped with a heating furnace.
mm, the sample was set, a constant load of 10 g was applied, and the temperature at which the elongation exceeded 1% (deformation start temperature) was measured while raising the temperature at 5 ° C./min.
° C. The thickness was 80 μm. Next, the ARTON film peeled from the PET film was heated at 125 ° C. for 1 hour.
Drying was performed at 50 ° C. at a line speed of 1 m / min. The residence time in each drying zone is 25 minutes. 150
A pair of nip rolls whose clearance was adjusted to 76 µm was provided in the drying zone at ° C. A 76.1 μm thick transparent optical norbornene resin film was obtained.

【0028】「比較例1」ニップロールのクリアランス
を全開(10mm)とした以外は実施例1と同じ操作に
よってフィルムを作成し、75.1μm厚の光学用透明
ノルボルネン系樹脂フィルムを得た。
Comparative Example 1 A film was prepared in the same manner as in Example 1 except that the nip roll clearance was fully opened (10 mm) to obtain a 75.1 μm thick transparent optical norbornene resin film.

【0029】「比較例2」ニップロールのクリアランス
を全開(10mm)とした以外は実施例2と同じ操作に
よってフィルムを作成し、76μm厚の光学用透明ノル
ボルネン系樹脂フィルムを得た。
Comparative Example 2 A film was prepared in the same manner as in Example 2 except that the nip roll clearance was fully opened (10 mm), to obtain a transparent optical norbornene resin film having a thickness of 76 μm.

【0030】「フィルムの評価」 (1)厚み測定 フィルムの端部より1mm間隔で厚みを測定し、「表
1」に示した。
"Evaluation of Film" (1) Measurement of Thickness The thickness was measured at 1 mm intervals from the edge of the film, and the results are shown in Table 1.

【0031】[0031]

【表1】 厚みバラツキ…最大厚み−最小厚み 厚みムラ…5mm離れたポイントでの厚み差の最大値[Table 1] Thickness variation ... maximum thickness-minimum thickness Thickness unevenness ... maximum thickness difference at a point 5mm away

【0032】(2)位相差ムラ 実施例、比較例のフィルムを延伸し、位相差の均一性を
評価し、「表2」に示した。 延伸条件 実施例1、比較例1:予熱ゾーン/延伸ゾーン/倍率
120℃/130℃/175% 実施例2、比較例2:予熱ゾーン/延伸ゾーン/倍率
140℃/150℃/175% 位相差測定 フィルム端部より1mm間隔で550nmにおけるレタデー
ションを測定した。
(2) Unevenness of retardation The films of Examples and Comparative Examples were stretched, and the uniformity of retardation was evaluated. The results are shown in Table 2. Stretching conditions Example 1, Comparative example 1: preheating zone / stretching zone / magnification
120 ° C / 130 ° C / 175% Example 2, Comparative Example 2: Preheating zone / stretching zone / magnification
140 ° C./150° C./175% retardation measurement Retardation at 550 nm was measured at 1 mm intervals from the edge of the film.

【0033】[0033]

【表2】 位相差バラツキ…最大位相差値−最小位相差値 位相差ムラ…5mm離れたポイントでの位相差値の差の最
大値 色斑観察…一対の透過軸が平行な偏光板間に偏光板の透
過軸と延伸フィルムの延伸軸とが約45度をなすように
配置し、これを拡散光源上に置き観察した。このとき、
スジ上の色斑が確認できなかったものは「○」、確認で
きるものは「×」とした。
[Table 2] Phase difference variance: Maximum phase difference value-Minimum phase difference value Phase difference unevenness: Maximum value of the difference in phase difference value at a point separated by 5 mm Color spot observation: Transmission of a polarizing plate between a pair of polarizing plates having a pair of transmission axes parallel to each other The axis and the stretching axis of the stretched film were arranged at about 45 degrees, and this was placed on a diffusion light source and observed. At this time,
A sample in which no color spots on the streaks could be confirmed was rated as “○”, and a sample in which color spots were confirmed was rated as “x”.

【0034】[0034]

【発明の効果】本発明により得られるノルボルネン系樹
脂フィルムは、厚みの均一性に優れ、位相差フィルムと
して利用する場合に局所的な位相差の変化を減少させる
ことが可能である。
The norbornene-based resin film obtained by the present invention has excellent thickness uniformity and can reduce local change in retardation when used as a retardation film.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 溶液キャスト法によるノルボルネン系樹
脂フィルムの製造方法において、乾燥工程の最後に、フ
ィルム変形開始温度以上であって変形開始温度+100
℃以下の温度範囲に設定された乾燥炉内において、得ら
れたフィルムを平均フィルム厚の95〜100%にクリ
アランスが設定された一対のニップロール間を通すこと
を特徴とするノルボルネン系樹脂フィルムの製造方法。
In a method for producing a norbornene-based resin film by a solution casting method, at the end of a drying step, the temperature is equal to or higher than the film deformation start temperature and the deformation start temperature is +100.
A norbornene-based resin film production characterized in that the obtained film is passed through a pair of nip rolls having a clearance set to 95 to 100% of the average film thickness in a drying furnace set to a temperature range of not more than ℃. Method.
JP35034399A 1999-12-09 1999-12-09 Method of producing norbornene based resin film Pending JP2001164000A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35034399A JP2001164000A (en) 1999-12-09 1999-12-09 Method of producing norbornene based resin film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35034399A JP2001164000A (en) 1999-12-09 1999-12-09 Method of producing norbornene based resin film

Publications (1)

Publication Number Publication Date
JP2001164000A true JP2001164000A (en) 2001-06-19

Family

ID=18409850

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35034399A Pending JP2001164000A (en) 1999-12-09 1999-12-09 Method of producing norbornene based resin film

Country Status (1)

Country Link
JP (1) JP2001164000A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002080649A (en) * 2000-09-08 2002-03-19 Mitsui Chemicals Inc Cycloolefinic polymer solution, and film or sheet obtained therefrom

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002080649A (en) * 2000-09-08 2002-03-19 Mitsui Chemicals Inc Cycloolefinic polymer solution, and film or sheet obtained therefrom

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