JPH0564821A - Casting film-forming method - Google Patents

Casting film-forming method

Info

Publication number
JPH0564821A
JPH0564821A JP25588691A JP25588691A JPH0564821A JP H0564821 A JPH0564821 A JP H0564821A JP 25588691 A JP25588691 A JP 25588691A JP 25588691 A JP25588691 A JP 25588691A JP H0564821 A JPH0564821 A JP H0564821A
Authority
JP
Japan
Prior art keywords
casting
film
molecular weight
polycarbonate
less
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
JP25588691A
Other languages
Japanese (ja)
Inventor
Toru Yoshida
透 吉田
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.)
Fujifilm Holdings Corp
Original Assignee
Fuji Photo Film 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 Fuji Photo Film Co Ltd filed Critical Fuji Photo Film Co Ltd
Priority to JP25588691A priority Critical patent/JPH0564821A/en
Publication of JPH0564821A publication Critical patent/JPH0564821A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide the method for forming polycarbonate film having excellent surface profile without developing surface irregularities, chalking and blushing and further film suitable for optical use such as phase difference. CONSTITUTION:As casting dope, polycarbonate having the intrinsic viscosity, which is not less than 0.8 and not more than 5.0, and the average molecular weight, which is not less than 40,000 and not more than 360,000 is employed and the casting is performed in the form of the dope having the concentration of solid content of 10-25%.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はポリカーボネートの流延
製膜方法に関する、特に光学的用途に用いる位相差板用
のポリカーボネートの流延製膜方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for casting a polycarbonate film, and more particularly to a method for casting a polycarbonate film for a retardation plate used for optical applications.

【0002】[0002]

【従来の技術】ポリカーボネートの製膜は、公知の製膜
手段、即ち溶液製膜法、溶融製膜法でフィルム又はシー
トに成形されている。従来溶解性や溶融性の観点から
か、分子量の低い、即ち極限粘度の低いポリカーボネー
ト樹脂が使用されている。例えば特開平2−59702
号公報には極限粘度0.35から0.7の範囲で規定し
ている。
2. Description of the Related Art A polycarbonate film is formed into a film or sheet by a known film forming means, that is, a solution film forming method or a melt film forming method. From the viewpoint of solubility and meltability, a polycarbonate resin having a low molecular weight, that is, a low intrinsic viscosity has been conventionally used. For example, JP-A-2-59702
In the gazette, the intrinsic viscosity is specified in the range of 0.35 to 0.7.

【0003】[0003]

【発明が解決しようとする課題】しかしながら上記のよ
うな極限粘度の原料を溶液として用いる場合、流延粘度
が低すぎると溶液流延には適さなくなるため、流延適性
粘度にするため、固形分濃度を上げたり、溶液温度を下
げ見掛けの粘度を上げる手段をとっている。しかしなが
ら固形分濃度が高くなると 流延時のレベリングが悪化して面ムラが発生し易
い。 高濃度の液を流延すると、条件により液の白濁化
か、流延時にブラッシングが発生し易い等の問題点があ
った。 又、溶液温度を下げることは、溶液の安定性,流延時の
乾燥への影響等種々の問題がある。本発明の目的は従来
の問題点を解消し、面ムラや白濁化及びブラッシングを
発生させることなく、面状況の優れたポリカーボネート
の流延製膜方法を提供することにある。更には、位相差
板のように光学的用途に適した膜を提供することにあ
る。
However, when a raw material having an intrinsic viscosity as described above is used as a solution, if the casting viscosity is too low, it becomes unsuitable for solution casting. Measures are taken to raise the concentration and lower the solution temperature to increase the apparent viscosity. However, when the solid content concentration is high, leveling during casting is deteriorated and surface unevenness is likely to occur. When a high-concentration liquid is cast, there are problems that the liquid becomes cloudy depending on conditions, or brushing easily occurs during casting. Further, lowering the solution temperature has various problems such as stability of the solution and influence on drying during casting. An object of the present invention is to solve the conventional problems, and to provide a polycarbonate casting film forming method in which the surface condition is excellent without causing surface unevenness, clouding and brushing. Furthermore, it is to provide a film suitable for optical applications such as a retardation plate.

【0004】[0004]

【課題を解決するための手段及び作用】本発明の上記目
的は、ポリカーボネートのメチレンクロライド溶液を金
属製の支持体上に流延して膜状物とした後、乾燥を行
い、該支持体上より剥取り、更に後乾燥を行う流延製膜
方法において、前記ポリカーボネートのメチレンクロラ
イド溶液としてポリカーボネートの極限粘度が0.8以
上,5.0以下、平均分子量4万以上36万以下のもの
を用い、固形分濃度10〜25%のドープとして流延す
ることを特徴とする流延製膜方法によって達成される。
The above object of the present invention is to cast a methylene chloride solution of a polycarbonate on a metal support to form a film, and then to dry the film on the support. In a casting film-forming method in which the polycarbonate is peeled off and further dried, a polycarbonate methylene chloride solution having an intrinsic viscosity of 0.8 or more and 5.0 or less and an average molecular weight of 40,000 or more and 360,000 or less is used. , A solid film having a solid content of 10 to 25% is cast.

【0005】本発明において、ポリカーボネートの極限
粘度0.8以上,5.0以下のものを用いるということ
は、平均分子量では4万以上36万以下に当たり、好ま
しくは極限粘度0.9以上,4.0以下(平均分子量で
は4.5万以上27万以下)、更に好ましくは極限粘度
0.95以上,3.0以下(平均分子量では4.8万以
上,19万以下)が良い。ここで平均分子量はSchn
ellの式によって求めた。即ち、平均分子量Mと極限
粘度(η)との間に次式の関係がある。〔η〕=1.23
×10-4×M0.83。分子量の高いものを溶液ドープにす
ることによって、分子量の低い場合と同一の溶液濃度で
あっても溶液の粘度が高くなるので、流延適性が良くな
る。ポリカーボネートの極限粘度0.8〜5.0とは、
0.8以下の場合は溶液粘度が低くなるため、固形分濃
度を上げる必要がある。通常の溶液濃度では流延粘度が
低くなりすぎ流延適性は低下する。5.0以上では逆に
溶液粘度が高すぎるため流延適性を持たせるためには溶
媒量を増さなければならないからである。又、本発明に
おいて、溶液の固形分濃度10〜25%のドープとして
流延するということは、好ましくは12〜22%であ
り、更に好ましくは15〜20%である。固形分濃度1
0%以下では溶媒量が多いため乾燥負荷から流延速度の
低下を来し、生産能率上好ましくなく、25%以上では
溶媒量が少ないことで流延時のレベリングが悪化し、白
濁や流延時のブラッシングの発生の危険性がある。更
に、ポリカーボネート膜を位相差板にするために延伸す
る場合において、極限粘度0.8以下の分子量の膜は、
分子の配向を持たせるために、延伸比率が大きくなる。
そのため延伸時のムラが目立ち、位相差板として適さな
い場合がある。又これを防止するために温度を上げたり
する。
In the present invention, the use of a polycarbonate having an intrinsic viscosity of 0.8 or more and 5.0 or less corresponds to an average molecular weight of 40,000 or more and 360,000 or less, preferably an intrinsic viscosity of 0.9 or more and 4. 0 or less (average molecular weight is 45,000 or more and 270,000 or less), and more preferably intrinsic viscosity is 0.95 or more and 3.0 or less (average molecular weight is 48,000 or more and 190,000 or less). Here, the average molecular weight is Schn
It was calculated by the formula of ell. That is, there is the following relationship between the average molecular weight M and the intrinsic viscosity (η). [Η] = 1.23
× 10 -4 × M 0.83 . By making a solution having a high molecular weight into a solution dope, the viscosity of the solution becomes high even if the solution concentration is the same as that of a case where the molecular weight is low, so that the casting aptitude is improved. What is the intrinsic viscosity of polycarbonate 0.8 to 5.0?
If it is 0.8 or less, the solution viscosity becomes low, and it is necessary to increase the solid content concentration. At a normal solution concentration, the casting viscosity becomes too low and the casting aptitude becomes poor. On the other hand, if it is 5.0 or more, the solution viscosity is too high, and therefore the amount of the solvent must be increased in order to have the castability. In the present invention, the casting as a dope having a solid content concentration of 10 to 25% is preferably 12 to 22%, more preferably 15 to 20%. Solid content concentration 1
When the amount is 0% or less, the amount of the solvent is large, and therefore the casting speed is reduced due to the drying load, which is not preferable in terms of production efficiency. When the amount is 25% or more, the amount of the solvent is small, the leveling at the time of casting is deteriorated, and the white turbidity or the time of casting is decreased. There is a risk of brushing. Furthermore, in the case of stretching the polycarbonate film to form a retardation plate, a film having a molecular weight of 0.8 or less is an intrinsic viscosity,
The stretching ratio is increased because the molecules are oriented.
Therefore, unevenness during stretching is conspicuous, and it may not be suitable as a retardation plate. To prevent this, the temperature is raised.

【0006】[0006]

【実施例】本発明を実施例を用いて説明する。但し、本
発明は本実施例に限定されることは無い。 (比較例−1)極限粘度0.457,分子量約2万のポ
リカーボネート樹脂をメチレンクロライドに溶解したと
ころ固形分濃度で17%で、33ポワズ(P)の粘度で
あった。これをダイより支持体上に流延したところ、粘
度が低すぎて、支持体上で流延幅が規定できず、ダイ流
延幅より広がってしまい、流延適性がなかった。そこで
固形分濃度を27%まで上げて粘度を122Pにした。
しかしこの状態では、液が白濁状になる上、流延しても
溶媒量が少なく、レベリングしにくくなり面ムラが発生
し、面質が悪かった。
EXAMPLES The present invention will be described with reference to examples. However, the present invention is not limited to this embodiment. (Comparative Example-1) A polycarbonate resin having an intrinsic viscosity of 0.457 and a molecular weight of about 20,000 was dissolved in methylene chloride to give a solid content of 17% and a viscosity of 33 poise (P). When this was cast on a support from a die, the viscosity was too low, the casting width could not be defined on the support, and it was wider than the die casting width, and was not suitable for casting. Therefore, the solid content concentration was increased to 27% and the viscosity was set to 122P.
However, in this state, the liquid became cloudy and the amount of the solvent was small even when the liquid was cast, so that leveling became difficult and surface unevenness occurred, resulting in poor surface quality.

【0007】(比較例−2)極限粘度5.5,分子量約
40万のポリカーボネート樹脂をメチレンクロライドに
溶解して固形分濃度12重量%の溶液としたが、固まり
状となって溶解できなかった。そこで8%まで濃度を下
げて溶解した。この時の粘度は1100Pであった。こ
の状態でも粘度が高いので更に濃度を下げ、6%にて流
延製膜した。支持体上へのダイからの吐出は問題なかっ
たが、濃度が低いため乾燥させる溶媒量が増え、流延速
度を5割も下げなければならず、生産効率上好ましくな
かった。又溶媒量も多量必要でコスト上も問題があっ
た。
(Comparative Example 2) A polycarbonate resin having an intrinsic viscosity of 5.5 and a molecular weight of about 400,000 was dissolved in methylene chloride to obtain a solution having a solid content of 12% by weight. .. Therefore, the concentration was lowered to 8% to dissolve. The viscosity at this time was 1100P. Since the viscosity is still high even in this state, the concentration was further lowered, and a casting film was formed at 6%. There was no problem in discharging from the die onto the support, but since the concentration was low, the amount of solvent to be dried increased, and the casting speed had to be reduced by 50%, which was not preferable in terms of production efficiency. In addition, a large amount of solvent is required, which is a cost problem.

【0008】(実施例−1)極限粘度0.85,分子量
約4.2万のポリカーボネート樹脂をメチレンクロライ
ドに溶解して固形分濃度20重量%の溶液とした。この
時の粘度は560Pであり、流延ダイから流す時に問題
なく流れ、且つ溶媒量も適当で、蒸発が増え、レベリン
グ効果も上がり、平面性がよかった。
Example 1 A polycarbonate resin having an intrinsic viscosity of 0.85 and a molecular weight of about 42,000 was dissolved in methylene chloride to obtain a solution having a solid content of 20% by weight. At this time, the viscosity was 560 P, and it flowed without problems when flowing from the casting die, the amount of solvent was appropriate, evaporation increased, the leveling effect improved, and the flatness was good.

【0009】(実施例−2)極限粘度1.30,分子量
約7万のポリカーボネート樹脂をメチレンクロライドに
溶解して固形分濃度17.8%の溶液にした。この時の
粘度は680Pあり、流延ダイから流す時に問題なく流
れ、かつ溶媒量も適当で蒸発が増え、ダイ周辺の溶媒蒸
気が満たされることでレベリング効果もあり、平面性が
よかった。
Example 2 A polycarbonate resin having an intrinsic viscosity of 1.30 and a molecular weight of about 70,000 was dissolved in methylene chloride to obtain a solution having a solid content of 17.8%. At this time, the viscosity was 680 P, and it flowed without problems when flowing from the casting die, the amount of solvent was appropriate and evaporation increased, and the solvent vapor around the die was filled with the leveling effect, and the flatness was good.

【0010】(実施例−3)極限粘度3.5(分子量約
23.2万)のポリカーボネート樹脂をメチレンクロラ
イドに溶解して、固形分濃度12.2重量%の溶液にし
た。この時の粘度は820Pであり、流延ダイから流す
時に問題なく流れ、かつ溶媒量も適当で蒸発が増え、レ
ベリング効果もあり、平面性が良かった。
Example 3 A polycarbonate resin having an intrinsic viscosity of 3.5 (molecular weight of about 232,000) was dissolved in methylene chloride to obtain a solution having a solid content concentration of 12.2% by weight. At this time, the viscosity was 820 P, and it flowed without problems when flowing from the casting die, the amount of solvent was appropriate, evaporation increased, and there was a leveling effect, and flatness was good.

【0011】本発明によって製作したポリカーボネート
フィルムの平面性がよかった。そこで、このフィルムを
延伸して比較したところ、分子量が高いことによって延
伸比率が低くても位相差が出やすいという結果が出た。
The flatness of the polycarbonate film produced according to the present invention was good. Then, when this film was stretched and compared, it was found that the retardation was likely to occur due to the high molecular weight even if the stretching ratio was low.

【0012】(比較例−3)極限粘度0.457,分子
量約2万のポリカーボネート樹脂の流延フィルムを延伸
し、位相差板にする時、レタデーションで570nmに
するのに170℃の状態で180%の延伸が必要であっ
た。延伸比が大きいために延伸ムラが目立ち品質的に劣
った。
(Comparative Example 3) When a cast film of a polycarbonate resin having an intrinsic viscosity of 0.457 and a molecular weight of about 20,000 was stretched to form a retardation plate, the retardation was 570 nm and the 180 ° C. at 180 ° C. % Stretching was required. Since the stretching ratio was large, unevenness in stretching was noticeable and the quality was poor.

【0013】(実施例−4)極限粘度0.95,分子量
約4.8万のボリカーボネート樹脂の流延フィルムを1
70℃で延伸した場合は、延伸比124%で同等のレタ
デーションになり、ムラもなく良好であった。又、極限
粘度1.3,分子量約7万のフィルムを170℃で延伸
した場合は、延伸比112%で同等のレタデーションに
なり、ムラもなく良好であった。更に又、極限粘度3.
5,分子量約23.2万のフィルムを170℃で延伸し
た場合は、延伸比108%で同等のレタデーションにな
りムラもなく良好であった。
(Example 4) A cast film of polycarbonate resin having an intrinsic viscosity of 0.95 and a molecular weight of about 48,000 was used as a film.
When stretched at 70 ° C., the same retardation was obtained at a stretch ratio of 124%, which was good without unevenness. Further, when a film having an intrinsic viscosity of 1.3 and a molecular weight of about 70,000 was stretched at 170 ° C., the retardation was 112% and the retardation was the same. Furthermore, the intrinsic viscosity is 3.
When a film having a molecular weight of about 232,000 was stretched at 170 ° C., the same retardation was obtained at a stretching ratio of 108%, which was good without unevenness.

【0014】[0014]

【発明の効果】本発明の流延製膜方法により、 平面性の優れたポリカーボネート膜を得ることが出
来た。 位相差膜として延伸した場合、位相差のムラの無い
優れた品質のものが得られた。本発明の方法によれば、
延伸比率は小さく出来て、又製膜流延設備に併設し、流
延と延伸とを一貫して行うことが出来る。
By the casting film forming method of the present invention, a polycarbonate film having excellent flatness can be obtained. When stretched as a retardation film, excellent quality with no unevenness in retardation was obtained. According to the method of the present invention,
The stretching ratio can be made small, and it is possible to perform casting and stretching consistently by installing it in the film forming casting equipment.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ポリカーボネートのメチレンクロライド
溶液を金属製の支持体上に流延して膜状物とした後、乾
燥を行い、該支持体上より剥取り、更に後乾燥を行う流
延製膜方法において、前記ポリカーボネートのメチレン
クロライド溶液としてポリカーボネートの極限粘度が
0.8以上,5.0以下、平均分子量4万以上36万以
下のものを用い、固形分濃度10〜25%のドープとし
て流延することを特徴とする流延製膜方法。
1. A casting film-forming method in which a methylene chloride solution of polycarbonate is cast onto a metal support to form a film, which is then dried, peeled off from the support, and further post-dried. In the method, a polycarbonate methylene chloride solution having a limiting viscosity of 0.8 or more and 5.0 or less and an average molecular weight of 40,000 or more and 360,000 or less is used as a dope having a solid content concentration of 10 to 25% and cast. A casting film forming method comprising:
JP25588691A 1991-09-09 1991-09-09 Casting film-forming method Pending JPH0564821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25588691A JPH0564821A (en) 1991-09-09 1991-09-09 Casting film-forming method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25588691A JPH0564821A (en) 1991-09-09 1991-09-09 Casting film-forming method

Publications (1)

Publication Number Publication Date
JPH0564821A true JPH0564821A (en) 1993-03-19

Family

ID=17284938

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25588691A Pending JPH0564821A (en) 1991-09-09 1991-09-09 Casting film-forming method

Country Status (1)

Country Link
JP (1) JPH0564821A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1369451A3 (en) * 2002-05-20 2004-02-04 Eastman Kodak Company Polycarbonate films prepared by coating methods

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1369451A3 (en) * 2002-05-20 2004-02-04 Eastman Kodak Company Polycarbonate films prepared by coating methods

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