JPH05245858A - Production of polyvinyl alcohol type film - Google Patents

Production of polyvinyl alcohol type film

Info

Publication number
JPH05245858A
JPH05245858A JP4654192A JP4654192A JPH05245858A JP H05245858 A JPH05245858 A JP H05245858A JP 4654192 A JP4654192 A JP 4654192A JP 4654192 A JP4654192 A JP 4654192A JP H05245858 A JPH05245858 A JP H05245858A
Authority
JP
Japan
Prior art keywords
film
polyvinyl alcohol
drying
heat treatment
temperature
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.)
Granted
Application number
JP4654192A
Other languages
Japanese (ja)
Other versions
JP3283564B2 (en
Inventor
Nobuo Tanaka
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
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Abstract

PURPOSE:To efficiently produce a polyvinyl alcohol type film suitable for the formation of a polarizing film excellent in physical properties capable of being subjected to various uses and especially excellent in both of polarizing characteristics and durability. CONSTITUTION:When a polyvinyl alcohol type film is formed from a polyvinyl alcohol type resin solution film using a film forming machine having a single surface drying type dryer constituted of one rotary body and the heat treatment device directly connecting said dryer, the film is transferred from a drying process to a heat treatment process at the point of time when the moisture content of the film reaches 2-15wt.% and heated at temp. higher than drying temp. to produce a polyvinyl alcohol type film wherein a product of hot water cutting temp. and a wt. swelling degree is 13000 or more.

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、各種用途に供しうる優れた物性を有
するポリビニルアルコール系フィルム、特に偏光性能と
耐久性に優れた偏光膜の作成に適したポリビニルアルコ
ール系フィルムを効率よく製造する方法に関する。
FIELD OF THE INVENTION The present invention relates to a method for producing a polyvinyl alcohol film. More specifically, the present invention is a method for efficiently producing a polyvinyl alcohol-based film having excellent physical properties that can be used in various applications, particularly a polyvinyl alcohol-based film suitable for producing a polarizing film having excellent polarization performance and durability. Regarding

【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 produced 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 it has 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 to have high quality and high reliability such as laptop personal computers, word processors, liquid crystal color projectors, in-vehicle navigation systems, and liquid crystal TVs from small devices such as calculators and watches in the early days. It is expanding to other devices. Under such circumstances, there is a demand for a polarizing film having both excellent polarization characteristics and durability that are far superior to those of conventional polarizing films. Therefore, in order to meet such a demand, for example, a method using a special dye, a method of forming a gel film of an organic solvent solution to produce a polyvinyl alcohol film as a base material, and the like have been proposed. However, these methods have drawbacks such that it is difficult to prepare a dye, and when an organic solvent is used, costs are inevitably increased in terms of safety and facility 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、各種用途に供しうる優れた物性を有する
ポリビニルアルコール系フィルム、特に優れた偏光特性
と耐久性とを併せもつ偏光膜の作成に適したポリビニル
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。
Under these circumstances, the present invention provides a polyvinyl alcohol film having excellent physical properties which can be used in various applications, and more particularly a polarizing film having both excellent polarization characteristics and durability. The present invention has been made for the purpose of providing a method for efficiently producing a polyvinyl alcohol film suitable for forming a film.

【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。
As a result of intensive studies to achieve the above-mentioned object, the present inventor has found that a single-sided drying type drying device constituted by one rotating body and a heat treatment device directly connected thereto are provided. By using a film forming machine having the same, the polyvinyl alcohol-based resin aqueous solution film is subjected to a drying treatment until a certain moisture content is obtained, and then subjected to a heat treatment at a higher temperature, so that the product of the hot water cutting temperature and the weight swelling degree is It was found that a polyvinyl alcohol film having a certain value or more was obtained, and 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
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, according to the present invention, a polyvinyl alcohol-based resin aqueous solution film is changed to a polyvinyl alcohol-based film using a film-forming machine having a single-sided drying type drying device composed of one rotating body and a heat treatment device directly connected thereto. In the production of the above, 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 film is heat treated at a temperature higher than the drying temperature. (° C) and weight swelling degree W
A method for producing a polyvinyl alcohol-based film having a product T × W (° C.%) of (%) of 13,000 or more is provided.

【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。このこのT×Wの値が13
000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、300rp
mで5分間遠心脱水した後の試料重量を(W1)、それ
を105℃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。
A polyvinyl alcohol film obtained by the method of the present invention (hereinafter, polyvinyl alcohol is referred to as PV
A, a polyvinyl alcohol film is abbreviated as PVA film) has a product T × W (° C.%) of hot water cutting temperature T (° C.) and weight swelling degree W (%) of 13000 or more, preferably 14000. As described above, more preferably 15000 or more. The value of this T × W is 13
If it is less than 000, it may not be possible to sufficiently exhibit the high polarization property and / or the high durability or both of them when used as a polarizing film. The method of measuring the weight swelling degree W (%) here is as follows. That is, 3 g of the sample film was cut into a width of about 3 mm, immersed in warm water at 30 ° C. for 15 minutes, and then cut at 300 rp.
The sample weight after spin-drying at m for 5 minutes (W1) and the sample weight after drying it at 105 ° C for 16 hours (W2)
Then, the weight swelling degree W (%) is calculated by the following equation. Weight swelling degree W (%) = (W1) / (W2) × 100 (I) Further, the method for measuring the hot water cutting temperature T (° C.) is as follows. That is, 0.5 g for a sample with a width of 5 mm and a length of 15 cm.
A weight of / 10 μm is attached and suspended in water at a temperature of 40 ° C., then the water temperature is raised at a rate of 3 ° C./minute, and the hot water temperature when the sample is cut is taken as the hot water cutting temperature T (° C.). Ask.

【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。
In the method of the present invention, the PVA-based film is prepared by using a film-forming machine having a single-sided drying type drying device composed of one rotating body and a heat treatment device directly connected to the drying device. When a PVA-based film is formed from the film, when the moisture content of the film reaches 2 to 15% by weight, preferably 3 to 10% by weight, the film is transferred from a drying step to a heat treatment step, and It is obtained by heat treatment at a high temperature. In the present invention, as the drying device, a one-sided drying type constituted by one rotating body is used. Specifically, a rotary heating drum, a rotary heating belt (or roll), or the like can be used. In these drying devices, the PVA-based resin aqueous solution film is not dried on the drum side (drum surface) and is opposite to the drum. Will be done only on the free side of. It is advantageous that 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 together, so that the drying efficiency is improved. The present invention requires a heat treatment device directly connected to the drying device, and a heating roll or a hot air oven 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,
It is preferably 70 to 120 ° C. 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 according to various situations, but is usually 80 to 140 ° C., preferably 100 to 1
It is 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 device 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, the surface of a metal rotary heating drum. The PVA-based resin aqueous solution film immediately enters a drying process, and the free surface side (the surface opposite to the drum) of the aqueous solution film is dried first. As the drying proceeds, the average moisture content of the entire film is 2 to 15% by weight, preferably 3 to 10%.
When the weight% is reached, the heat treatment step is performed. 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. Since the PVA-based film usually reaches the absolute dryness after the heat treatment process, the PVA film to which the desired water content has been imparted is subjected to the humidity conditioning treatment thereafter.
A system 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。
P when transferring from the drying step to the heat treatment step
When the water content of the VA-based film is less than 2% by weight or more than 15% by weight, neither of them has high polarization and high durability, and the object of the present invention cannot be achieved. The reason why the PVA film thus obtained exhibits high polarization characteristics is presumed as follows. That is, the PVA
When the film is transferred from the drying process to the heat treatment process, the water content (total thickness average) of the entire film is 2 to 15% by weight, but it differs depending on the position in the thickness direction, and the dryness progresses on the free surface side. 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, which has a high moisture content, progresses, but crystallization on the free surface side, which has almost no moisture, progresses little. As a result, the film has low crystallinity and therefore has one side with high weight swelling (free side) and the other side with high crystallinity and high hot water cutting temperature (drum side). As a result, it is estimated that the product of the weight swelling degree of the PVA-based film and the hot water cutting temperature was increased.
In addition, when a polarizing film is formed from this film, excellent dyeing properties on one side, orientation at the time of stretching, and excellent hot water resistance on the other side, that is, excellent high-temperature stretchability, are combined, resulting in high polarization. It is presumed that the characteristics and high durability are exhibited.

【0010】このようにして得られたPVA系フィルム
は、各種の用途に適したものであり、特に偏光膜に最適
である。このPVA系フィルムを用いて偏光膜を製造す
るには、公知の方法、例えばPVA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。
The PVA-based film thus obtained is suitable for various uses, and is most suitable for a polarizing film. To produce a polarizing film using this PVA-based film, a known method, for example, dyeing with a PVA-based film,
It is possible to use a method of producing a polarizing film by performing stretching, treatment with a boric acid compound, etc., and then drying. The dyeing may be performed before, during or after the uniaxial stretching, and as the dye, for example, iodine-potassium iodide or a dichroic dye may be used. The stretching may be carried out in warm water, or the film after absorbing water may be carried out in air, and the stretching temperature is usually 30 ° C. or higher, preferably 40 ° C. or higher, more preferably 50 ° C. or higher. Furthermore, in the boric acid compound treatment,
You may mix an iodine compound in a boric acid compound bath. The polarizing film thus obtained is usually laminated with various supports such as 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 resin that can be used in the present invention is a so-called ordinary PVA produced by saponifying polyvinyl acetate obtained by polymerizing vinyl acetate.
In addition, unsaturated carboxylic acid or its derivative, unsaturated sulfonic acid or its derivative, modified polyvinyl alcohol copolymerized with less than about 15 mol% of α-olefin having 2 to 30 carbon atoms, or polyvinyl formal or polyvinyl acetoacetal Examples thereof include polyvinyl acetals such as polyvinyl butyral and ethylene-vinyl alcohol copolymers 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 preferable because they have excellent polarization characteristics and durability. The degree of saponification of the PVA-based resin is 90 mol% or more, preferably 95 mol% or more, more preferably 98 mol% or more, which is excellent in durability and desirable. As the solvent for producing the PVA-based film in the present invention, water, an organic solvent, or a mixture thereof can be used. However, the present invention is a water-only solvent system having high polarization characteristics and high durability. The feature is that a system film can be obtained, and 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
It is selected in the range of 100 μm. In addition, various polyol plasticizers such as glycerin and additive components such as nonionic, anionic and cationic surfactants may be appropriately added to the PVA-based film, if desired.

【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。
The present invention will be described in more detail by way of examples, which should not be construed as limiting the invention thereto. In addition, in Examples and Comparative Examples, the moisture content of the film is the weight of the film sample before drying (G
1) When the weight after vacuum drying at 50 ° C. for 16 hours is (G2), the moisture content of the film (%) = (G1−G2) / G1 × 100 ... (II). Further, common manufacturing conditions in the polarizing film manufacturing process are as follows. That is, the dye concentration of the dyeing bath was fixed at an iodine / potassium iodide weight ratio of 1/10, and the iodine concentration was appropriately selected within the range of 1 to 20 g / liter to prepare a polarizing film having a single transmittance of about 43%. It was collected. The boric acid concentration in the boric acid bath was set to 4% by weight, and boric acid was added to the drawing bath so that the concentration was 4% by weight. Dry 5
It 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. This dichroic ratio is calculated from the light transmittance (single transmittance) Ts (%) of the polarizing film and the polarization degree P (%) according to the formula: dichroic ratio = log (Ts / 100-Ts × P / 10000) / log ( Ts / 100 + Ts × P / 10000) ・ ・ ・ (III) Further, the durability was evaluated by using a polarizing plate obtained by adhering cellulose triacetate having a thickness of 80 μm on both sides of a polarizing film using a PVA adhesive, in an atmosphere of a temperature of 60 ° C. and a relative humidity (RH) of 90%. It was performed by measuring the single-body transmittance and the degree of polarization after standing for 200 hours underneath.

【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 prepared by using a film-forming machine comprising an extruder, a die, a single rotary heating metal drum whose periphery is covered with a hot air oven, and a hot air oven type heat treatment device. Temperature 7
5 ℃, hot air temperature 75 ℃, heat treatment equipment hot air temperature 12
It was set to 0 ° C. A pellet consisting of 41 parts by weight of PVA having a degree of polymerization of 1700 and a degree of saponification 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 and dried and heat-treated continuously to obtain a P film having a thickness of 75 μm.
A VA film was created. The weight swelling degree of the obtained film was 210% and the hot water cutting temperature was 65 ° C., and therefore the product of the weight swelling degree and the hot water cutting temperature was 13650. The water content of the film taken 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. Maximum water temperature at which stretching is possible (hereinafter abbreviated as maximum water temperature during stretching)
The film was uniaxially stretched under the conditions of 35 ° C. and the upper limit of draw ratio (hereinafter abbreviated as upper limit draw ratio) of 5.3 times. The obtained polarizing film has a single transmittance of 43.3% and a polarization degree of 98.8%.
The dichroic ratio was 35.1, which was excellent in 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 hot air temperature was set to 90 ° C., and the hot air temperature of the heat treatment apparatus was set to 120 ° C. Saponification degree of polymerization degree 4000 9.
Pellet consisting of 35 parts by weight of 6 mol% PVA, 60 parts by weight of water and 5 parts by weight of glycerin was cast on a rotating heated metal drum, dried and heat-treated continuously to give a film thickness of 7
A 5 μm PVA film was created. The weight swelling degree of the obtained film was 215%, the hot water cutting temperature was 70 ° C., and therefore the product of the weight swelling degree and the hot water cutting temperature was 15050. The water content of the film taken 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 dyed, stretched, treated with boric acid and dried in order to prepare a polarizing film. The film was uniaxially stretched under the conditions of an upper limit water temperature of 50 ° C. and an upper limit draw ratio of 5.0 times. The obtained polarizing film had a simple transmittance of 43.2%, a polarization degree of 99.7%, and a dichroic ratio of 45.0, and had excellent polarization performance. After the durability test of this polarizing film, the single transmittance was 47.3%, the degree of polarization was 93.6%, and the dichroic ratio was 39.7, showing 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 rotary heating metal drum temperature was set to 70 ° C., the hot air temperature was set to 70 ° C., and the hot air temperature of the heat treatment device was set to 150 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and dried and heat-treated continuously to prepare a PVA film having a film thickness of 75 μm. The weight swelling degree 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 water content of the film taken between the drying device and the heat treatment device was 4.4% by weight.
Next, this film was sequentially subjected to dyeing, stretching, boric acid treatment and drying to form a polarizing film. Maximum water temperature during stretching 50
The film was uniaxially stretched under conditions of a temperature of ℃ and a maximum draw ratio of 4.4 times. The obtained polarizing film has a single transmittance of 42.6% and a polarization degree of 94.6.
%, The dichroic ratio was 20.1, and the polarization performance was poor.

【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 rotating heating metal drum temperature was set to 85 ° C., the hot air temperature was set to 85 ° C., and the hot air temperature of the heat treatment device was set to 120 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and dried and heat-treated continuously to prepare a PVA film having a film thickness of 75 μm. The weight swelling degree of the obtained film was 205%, the hot water cutting temperature was 62 ° C., and therefore the product of the weight swelling degree and the hot water cutting temperature was 12710. The water content of the film taken between the drying device and the heat treatment device was 0.8% by weight.
Next, this film was sequentially subjected to dyeing, stretching, boric acid treatment and drying to form a polarizing film. Maximum water temperature during stretching 30
The film was uniaxially stretched at a temperature of ℃ and a maximum draw ratio of 4.5. The obtained polarizing film has a single transmittance of 43.0% and a polarization degree of 92.6.
%, The dichroic ratio was 18.3, and the polarization performance was inferior.

【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 rotary heating metal drum temperature was set to 50 ° C., the hot air temperature was set to 50 ° C., and the hot air temperature of the heat treatment device was set to 120 ° C. The same pellets as in Example 1 were cast on a rotary heating metal drum, and dried and heat-treated continuously to prepare a PVA film having a film thickness of 75 μm. The weight swelling degree of the obtained film was 180%, the hot water cutting temperature was 67 ° C., and therefore the product of the weight swelling degree and the hot water cutting temperature was 12060. The water content of the film taken between the drying device and the heat treatment device was 20.6% by weight. Next, this film was sequentially subjected to dyeing, stretching, boric acid treatment and drying 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 times.
The resulting polarizing film has a single transmittance of 44.3% and a polarization degree of 93.
The dichroic ratio was 8%, and the dichroic ratio was 23.6, which was inferior in polarization performance.

【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 rotary heating metal drum temperature was set to 90 ° C. and the hot air temperature was set to 90 ° C., the same pellets as in Example 2 were used for casting, and only drying was performed. Go to 7
An unheated PVA film of 5 μm was obtained. The water content of this film was 8.5% by weight. After leaving this film roll for 1 day, it was heat-treated using the same heat-treatment device as in Example 1 to obtain a heat-treated PVA film. The obtained film had a weight swelling degree of 177% and a hot water cutting temperature of 71.
℃, therefore the product of the weight swelling degree and the hot water cutting temperature is 12
It was 567. Next, this film was sequentially subjected to dyeing, stretching, boric acid treatment and drying to form a polarizing film. The film was uniaxially stretched under the conditions of the upper limit water temperature of 50 ° C. and the upper limit stretch ratio of 4.4 times. The single transmittance of the obtained polarizing film is 43.6%,
The polarization degree 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、様々な物性のす
ぐれたPVA系フィルム、特に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, a PVA-based film having various excellent physical properties, particularly a PVA-based film excellent in the production of a polarizing film having extremely excellent polarization characteristics and durability, can be easily obtained. The polarizing film obtained from this PVA-based film can be sufficiently applied to the LCD field for which characteristics higher than those of the conventional polarizing film are required, such as those for personal computers, word processors, and televisions.

Claims (1)

【特許請求の範囲】[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以上であるポリビニルアルコー
ル系フィルムの製造方法。
1. When manufacturing 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 composed of one rotating body and a heat treatment device directly connected to the drying device. A hot water cutting temperature T (° C.), characterized in that the film is transferred from the drying step to the heat treatment step when the moisture content of the film reaches 2 to 15% by weight, and heat treatment is performed at a temperature higher than the drying temperature. Product T × W with the degree of weight swelling W (%)
A method for producing a polyvinyl alcohol-based film having a (° C ·%) of 13,000 or more.
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 true JPH05245858A (en) 1993-09-24
JP3283564B2 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)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001315143A (en) * 2000-05-12 2001-11-13 Kuraray Co Ltd Method for manufacturing polyvinyl alcohol film
JP2002144418A (en) * 2000-11-15 2002-05-21 Kuraray Co Ltd Method for cutting vinyl alcohol polymer film for stretch processing and polarizing film
EP1153962A3 (en) * 2000-05-01 2002-06-26 Kuraray Co., Ltd. Polyvinyl alcohol polymer film and polarization film
JP2006305923A (en) * 2005-04-28 2006-11-09 Nippon Synthetic Chem Ind Co Ltd:The Polyvinyl alcohol film, its manufacturing method, polarizing film and polarizing plate
KR100818135B1 (en) * 2000-05-12 2008-03-31 가부시키가이샤 구라레 Polyvinyl alcohol film and polarization film
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JP2010253952A (en) * 2010-05-14 2010-11-11 Kuraray Co Ltd Method for cutting vinyl alcohol-based polymer film for stretching process
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KR20160089349A (en) 2013-11-21 2016-07-27 주식회사 쿠라레 Polyvinyl alcohol film
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EP1153962A3 (en) * 2000-05-01 2002-06-26 Kuraray Co., Ltd. Polyvinyl alcohol polymer film and polarization film
EP1690891A1 (en) * 2000-05-01 2006-08-16 Kuraray Co., Ltd., Kurashiki Plant Polyvinyl alcohol polymer film and polarization film
US7511093B2 (en) 2000-05-01 2009-03-31 Kuraray Co., Ltd. Polyvinyl alcohol polymer film and polarization film
KR100818135B1 (en) * 2000-05-12 2008-03-31 가부시키가이샤 구라레 Polyvinyl alcohol film and polarization film
JP2001315143A (en) * 2000-05-12 2001-11-13 Kuraray Co Ltd Method for manufacturing polyvinyl alcohol film
JP4646356B2 (en) * 2000-05-12 2011-03-09 株式会社クラレ Production method of polyvinyl alcohol film
JP2002144418A (en) * 2000-11-15 2002-05-21 Kuraray Co Ltd Method for cutting vinyl alcohol polymer film for stretch processing and polarizing film
JP2006305923A (en) * 2005-04-28 2006-11-09 Nippon Synthetic Chem Ind Co Ltd:The Polyvinyl alcohol film, its manufacturing method, polarizing film and polarizing plate
JP5628025B2 (en) * 2008-12-18 2014-11-19 株式会社クラレ Polyvinyl alcohol film
WO2010071094A1 (en) * 2008-12-18 2010-06-24 株式会社クラレ Polyvinyl alcohol film
KR20110105803A (en) * 2008-12-18 2011-09-27 가부시키가이샤 구라레 Polyvinyl alcohol film
JPWO2010071094A1 (en) * 2008-12-18 2012-05-31 株式会社クラレ Polyvinyl alcohol film
JP2010253952A (en) * 2010-05-14 2010-11-11 Kuraray Co Ltd Method for cutting vinyl alcohol-based polymer film for stretching process
JP2013227544A (en) * 2012-03-30 2013-11-07 Kuraray Co Ltd Film roll and package thereof
KR20160089349A (en) 2013-11-21 2016-07-27 주식회사 쿠라레 Polyvinyl alcohol film
WO2017029881A1 (en) * 2015-08-18 2017-02-23 日本合成化学工業株式会社 Polyvinyl alcohol film, and polarizing film in which same is used
JPWO2017029881A1 (en) * 2015-08-18 2018-06-07 日本合成化学工業株式会社 Polyvinyl alcohol film and polarizing film using the same

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