JPH1149876A - Highly rigid heat-resistant aramide film - Google Patents
Highly rigid heat-resistant aramide filmInfo
- Publication number
- JPH1149876A JPH1149876A JP21082097A JP21082097A JPH1149876A JP H1149876 A JPH1149876 A JP H1149876A JP 21082097 A JP21082097 A JP 21082097A JP 21082097 A JP21082097 A JP 21082097A JP H1149876 A JPH1149876 A JP H1149876A
- Authority
- JP
- Japan
- Prior art keywords
- film
- washed
- heat
- ppm
- aramid
- 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
Links
Classifications
-
- H—ELECTRICITY
- H05—ELECTRIC TECHNIQUES NOT OTHERWISE PROVIDED FOR
- H05K—PRINTED CIRCUITS; CASINGS OR CONSTRUCTIONAL DETAILS OF ELECTRIC APPARATUS; MANUFACTURE OF ASSEMBLAGES OF ELECTRICAL COMPONENTS
- H05K1/00—Printed circuits
- H05K1/02—Details
- H05K1/03—Use of materials for the substrate
- H05K1/0313—Organic insulating material
- H05K1/032—Organic insulating material consisting of one material
- H05K1/0346—Organic insulating material consisting of one material containing N
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Polyamides (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、高剛性耐熱アラミドフ
ィルムに関するものであり、さらに詳しくは、フィルム
として特別な要件を備えているが故に優れた耐湿熱性を
有する高剛性耐熱アラミドフィルムに関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a high-rigid heat-resistant aramid film, and more particularly, to a high-rigid heat-resistant aramid film having excellent moisture and heat resistance because of special requirements as a film. is there.
【0002】[0002]
【従来技術】アラミドフィルムは、高いヤング率をもつ
高剛性の耐熱性フィルムとして注目されており、磁気テ
ープ、プリンター用インクシート、太陽電池用ベースフ
ィルム、フレキシブルプリント配線板用フィルム、電気
絶縁用フィルム、音響材などとして実用化が始まってい
る。2. Description of the Related Art Aramid films are attracting attention as high-rigidity heat-resistant films having a high Young's modulus, such as magnetic tapes, ink sheets for printers, base films for solar cells, films for flexible printed wiring boards, and films for electrical insulation. Practical use has begun as an acoustic material.
【0003】これらのいくつかの用途において、高温高
湿の環境で使用される場合があるが、従来のアラミドフ
ィルムは、このような環境下または/及びこのような環
境での使用後に、機械的・電気的性質の低下、他の材料
との接着力の低下があったり、フィルムの平坦性や一直
性が損なわれたりすることが多く、使用上の制限を受け
てきた。In some of these applications, the aramid film may be used in a high temperature and high humidity environment, but the conventional aramid film may not be used in such an environment or / and after use in such an environment. -In many cases, the electrical properties are reduced, the adhesive strength to other materials is reduced, and the flatness and straightness of the film are often impaired, so that use of the film has been limited.
【0004】特開昭50−102650号公報、特開昭
51−81854号公報には、カールの少ないつまり平
坦性のよいアラミドフィルムを得るためにイオン性無機
化合物含量を少なくすることが開示されている。しか
し、これらは通常の状態での平坦性に関するもので、耐
湿熱性の改良を意図したものではなく、実際湿熱処理に
よる諸性能の低下が大きい。JP-A-50-102650 and JP-A-51-81854 disclose that the content of an ionic inorganic compound is reduced in order to obtain an aramid film having less curl, that is, good flatness. I have. However, these are related to flatness in a normal state, and are not intended to improve wet heat resistance. Actually, various heat treatments cause a large decrease in performance.
【0005】特開昭63−141207号公報には、ア
ラミドフィルムの耐熱性・耐引裂性を改善するために、
アラミドに化学結合した塩素及び化学結合せずに含有さ
れる塩素の合計含量が特定値以下のアラミドフィルムが
開示されている。しかし、これに開示されたフィルムも
耐湿熱性の改良が意図されていず、実際耐湿熱性は不十
分である。JP-A-63-141207 discloses a method for improving the heat resistance and tear resistance of an aramid film.
An aramid film in which the total content of chlorine chemically bonded to aramid and chlorine contained without chemical bonding is equal to or less than a specific value is disclosed. However, the films disclosed therein are not intended to improve the wet heat resistance, and in fact, have insufficient wet heat resistance.
【0006】[0006]
【発明が解決しようとする課題】本発明の課題は、従来
のアラミドフィルムのもっている欠点、特に耐湿熱欠点
の解消されたフィルムの提供、即ち、湿熱処理を受けて
も、フィルム自体の機械的性質、電気的性質、他の材料
との接着力の低下が少なく、またフィルムの平坦性及び
一直性の維持された高剛性耐熱フィルムを提供すること
にある。SUMMARY OF THE INVENTION An object of the present invention is to provide a film in which the disadvantages of the conventional aramid film, in particular, the resistance to moisture and heat, have been eliminated, that is, even if the film itself is subjected to a wet heat treatment, the mechanical properties of the film itself are reduced. An object of the present invention is to provide a high-rigidity heat-resistant film in which the properties, electrical properties, and adhesion to other materials are hardly reduced, and the flatness and straightness of the film are maintained.
【0007】[0007]
【発明が解決しようとする課題】本発明者は、この課題
を解決するために種々の観点から検討するうちに、耐湿
熱性にはアラミドフィルム中に微量含有されていること
の多い塩素が強く関与していること、特にアラミド分子
に化学結合していない微量の塩素の影響が大きいという
予想外の事実を発見し、更に詳しい検討を加えて本発明
に到達したものである。The inventors of the present invention have studied from various viewpoints to solve this problem. As a result, the moisture and heat resistance strongly involves chlorine, which is often contained in a small amount in the aramid film. In particular, the present inventors have discovered an unexpected fact that the effect of a trace amount of chlorine not chemically bonded to the aramid molecule is large, and reached the present invention after further detailed investigation.
【0008】すなわち、本発明は、ヤング率が700〜
2500kg/mm2のアラミドフィルムにおいて、洗
浄抽出される塩素量が0.001〜8ppmであること
を特徴とする高剛性耐熱アラミドフィルムである。以
下、本発明を詳細に説明する。That is, according to the present invention, the Young's modulus is 700 to
A high-rigidity heat-resistant aramid film characterized in that the amount of chlorine extracted and washed in a 2500 kg / mm 2 aramid film is 0.001 to 8 ppm. Hereinafter, the present invention will be described in detail.
【0009】本発明に用いられるアラミドとしては、次
の構成単位からなる群より選択された単位より実質的に
構成される。 −NH−Ar1−NH− (1) −CO−Ar2−CO− (2) −NH−Ar3−CO− (3) ここでAr1、Ar2、Ar3は少なくとも1個の芳香環
を含み、同一でも異なっていてもよく、これらの代表例
としては、下記式で示される構造のものが挙げられる。The aramid used in the present invention is substantially composed of units selected from the group consisting of the following structural units. —NH—Ar 1 —NH— (1) —CO—Ar 2 —CO— (2) —NH—Ar 3 —CO— (3) where Ar 1 , Ar 2 and Ar 3 are at least one aromatic ring And may be the same or different. Representative examples thereof include those represented by the following formula.
【0010】[0010]
【化1】 Embedded image
【0011】また、これらの芳香環の環上の水素の一部
が、ハロゲン基、ニトロ基、アルキル基、アルコキシ基
などで置換されているものも含む。また、Xは−O−、
−CH2−、−SO2−、−S−、−CO−などである。
特に、全ての芳香環の80モル%以上がパラ位にて結合
されているアラミドが好ましい。[0011] Further, those in which a part of hydrogen on the ring of these aromatic rings is substituted with a halogen group, a nitro group, an alkyl group, an alkoxy group or the like are also included. X is -O-,
—CH 2 —, —SO 2 —, —S—, —CO— and the like.
In particular, an aramid in which 80 mol% or more of all the aromatic rings are bonded at the para position is preferable.
【0012】また、本発明のアラミドフィルムには、フ
ィルムの物性を損ねたり、本発明の目的に反しない限
り、つまり塩素化合物を含まない限り、易滑剤、酸化防
止剤、その他の添加剤などや、他のポリマーが含まれて
いてもよい。本発明のフィルムのヤング率は700〜2
500kg/mm2であるべきで、好ましくは900〜
2500kg/mm2である。ヤング率が700kg/
mm2未満のフィルムは、もはや高剛性フィルムという
範ちゅうのフィルムでなくなるからである。一方、25
00kg/mm2を超えるアラミドフィルムは、裂け易
く且つ脆くなって、もはやフィルムとしての有用性が少
なくなってしまうからである。The aramid film of the present invention may contain a lubricant, an antioxidant, other additives, etc. as long as the physical properties of the film are not impaired or the object of the present invention is not adversely affected, that is, unless a chlorine compound is contained. , And other polymers may be included. The Young's modulus of the film of the present invention is 700 to 2
Should be 500 kg / mm 2 , preferably 900 to
2500 kg / mm 2 . Young's modulus is 700kg /
This is because a film having a size of less than mm 2 is no longer a film in the category of a highly rigid film. On the other hand, 25
This is because an aramid film exceeding 00 kg / mm 2 is easily torn and brittle, and its usefulness as a film is reduced.
【0013】本発明の高ヤング率のフィルムは、分子構
造的にパラ配向成分を多くすること、製造時に相対的に
高い延伸倍率を適用して、分子鎖を高配向化することで
実現できる。本発明は、物性がフィルム面内の全方向に
一定のいわゆるバランスタイプには勿論のこと、長さ方
向または幅方向に強化されたテンシライズドタイプにも
適用することが出来る。The film having a high Young's modulus of the present invention can be realized by increasing the number of para-oriented components in the molecular structure and by applying a relatively high stretching ratio at the time of production to make the molecular chains highly oriented. The present invention can be applied not only to a so-called balance type in which the physical properties are constant in all directions in the film plane, but also to a tensile type in which the length direction or the width direction is reinforced.
【0014】本発明において、フィルム中に含有される
洗浄抽出される塩素量が0.001〜8ppmであるこ
とが肝要である。ここで、洗浄抽出される塩素とは、ア
ラミドポリマーに化学結合していない塩素のことであ
り、塩化水素、塩化ナトリウム、塩化リチウム、塩化カ
ルシウム、塩化マグネシウムなどの形でフィルム中に存
在する塩素の総量を指す。アラミドは、一般に、芳香族
ジアミンと芳香族ジカルボン酸クロライドとからの塩化
水素副生の重縮合反応で得られるため、反応終了後の通
常の工業的な中和、洗浄、抽出による塩化水素の分離、
除去を行っても塩素の残存が避けられず、約20ppm
以下のポリマー非結合性塩素含量にすることは極めて困
難である。このため、前記の範囲の洗浄抽出される塩素
含有量にするには、後述する特別の処理をする必要があ
る。フィルム中の洗浄抽出される塩素含量が8ppmを
超えると、フィルムの耐湿熱性が極端に低下する。即
ち、フィルムを湿熱処理する場合、例えば、50℃、8
0%RHで1週間放置したときや100℃90%RHで
一日放置したとき、処理後のフィルムの機械的性質の低
下、接着力の低下、平坦性(平面性)の悪化、一直性の
悪化(フィルムの湾曲)等が起こる。In the present invention, it is important that the amount of chlorine contained in the film to be washed and extracted is 0.001 to 8 ppm. Here, the chlorine extracted by washing is chlorine that is not chemically bonded to the aramid polymer, and is the chlorine present in the film in the form of hydrogen chloride, sodium chloride, lithium chloride, calcium chloride, magnesium chloride, etc. Refers to the total amount. Aramid is generally obtained by a polycondensation reaction of by-produced hydrogen chloride from an aromatic diamine and an aromatic dicarboxylic acid chloride, so that hydrogen chloride is separated by ordinary industrial neutralization, washing and extraction after the reaction is completed. ,
Chlorine remains unavoidable even after removal, about 20 ppm
It is extremely difficult to achieve the following non-polymerizable chlorine content: For this reason, it is necessary to perform a special treatment described later in order to make the chlorine content in the above range that is extracted by washing. If the chlorine content of the film to be washed and extracted exceeds 8 ppm, the wet heat resistance of the film is extremely reduced. That is, when the film is subjected to wet heat treatment, for example, 50 ° C., 8
When left at 0% RH for 1 week or at 100 ° C. and 90% RH for 1 day, the mechanical properties of the treated film are reduced, the adhesive strength is reduced, the flatness (flatness) is deteriorated, and the linearity is reduced. Deterioration (curvature of the film) and the like occur.
【0015】フィルム中の洗浄抽出される塩素含有量の
上限は好ましくは5ppmである。フィルム中の洗浄抽
出される塩素含有量は少なければ少ないほど耐湿熱性は
良好になるが、工業的な実施の限界から下限値を0.0
01ppmとした。本発明のフィルムは、その密度が
1.40〜1.47g/cm3の範囲にあるのが耐湿熱
性を一層高める上で好ましい。アラミドフィルムにおい
て、この範囲の密度を持つことは、高結晶性で緻密であ
ることを意味している。密度の測定は、例えば、四塩化
炭素/トルエン中25℃でいわゆる密度勾配管法によっ
て行うことが出来、実際後述の本発明の実施例のフィル
ムは全て1.41〜1.46g/cm3の密度をもって
いた。[0015] The upper limit of the chlorine content of the film to be washed and extracted is preferably 5 ppm. The lower the chlorine content of the film extracted and washed, the better the moist heat resistance, but the lower limit is set at 0.0 from the limit of industrial practice.
01 ppm. The film of the present invention preferably has a density in the range of 1.40 to 1.47 g / cm 3 in order to further increase the wet heat resistance. In the aramid film, having a density in this range means that the film is highly crystalline and dense. The density can be measured, for example, by a so-called density gradient tube method at 25 ° C. in carbon tetrachloride / toluene. In fact, all the films of Examples of the present invention described below have a density of 1.41 to 1.46 g / cm 3 . Had a density.
【0016】また、フィルムにおける密度のバラツキが
0.01以下であることが、湿熱処理後のフィルムの平
坦性を良好な状態に保つ上で好ましく、実際後述の本発
明の実施例のフィルムは全て0〜0.01g/cm3の
密度のバラツキであった。密度のバラツキは、フィルム
の任意の場所で図った測定値10点での最大値と最小値
の差で定義される。It is preferable that the variation in the density of the film be 0.01 or less in order to keep the flatness of the film after the wet heat treatment in a good state. The density varied from 0 to 0.01 g / cm 3 . The variation in density is defined as the difference between the maximum value and the minimum value at 10 measured values measured at an arbitrary position on the film.
【0017】本発明は、平均厚みが約1〜1000μm
のフィルムに適用できるが、平均厚みに対する厚みばら
つきの比が0〜5%であることが好ましい。更に好まし
くは、この比は0〜4%である。比が5%を超えると、
フィルムをロール状に捲上げたときフィルムの捲姿が悪
くなり、ロールからの解除そのものや解除後のフィルム
の加工性が悪くなるからである。According to the present invention, the average thickness is about 1 to 1000 μm.
However, the ratio of the thickness variation to the average thickness is preferably 0 to 5%. More preferably, this ratio is 0-4%. If the ratio exceeds 5%,
This is because, when the film is wound up in a roll, the winding appearance of the film becomes poor, and the release itself from the roll and the workability of the film after the release become poor.
【0018】本発明のフィルムは、好ましくは、30〜
80kg/mm2の強度を持っており、これは一般のフ
ィルムに比べて相当に高い強度であり、高剛性フィルム
に関連した特徴の一つである。本発明のフィルムは、ま
た、好ましくは、15〜100%の伸度を持っている。
15%未満の伸度のフィルムは脆いことが往々にして見
られるからである。一方、伸度は一般に大きい方が望ま
しいが、高剛性フィルムにあっては、実際的には100
%程度が上限になる。伸度は、ポリマーの重合度や延伸
配向度、結晶化度等の調整によって達成できる。The film of the present invention preferably has a thickness of 30 to
It has a strength of 80 kg / mm 2 , which is considerably higher than that of a general film, and is one of the features related to a high-rigidity film. The films of the present invention also preferably have an elongation of 15 to 100%.
This is because films with an elongation of less than 15% are often found to be brittle. On the other hand, it is generally desirable that the elongation is large.
% Is the upper limit. The elongation can be achieved by adjusting the degree of polymerization, the degree of stretching orientation, the degree of crystallization, and the like of the polymer.
【0019】本発明のフィルムは、更に、フィルム面方
向の吸湿膨張係数が0〜40ppm/%RHであるのが
好ましく、更に好ましくは0〜25ppm/%RHであ
る。フィルム面方向の吸湿膨張係数が大きすぎると、湿
度変化に対する寸法変化が大きくなり、フィルムの取扱
い、加工性、各用途での性能の変化等を結果して好まし
くない。The film of the present invention further preferably has a coefficient of hygroscopic expansion in the film surface direction of 0 to 40 ppm /% RH, more preferably 0 to 25 ppm /% RH. If the coefficient of hygroscopic expansion in the direction of the film surface is too large, the dimensional change with respect to the change in humidity increases, which is not preferable because the handling of the film, the processability, and the performance in each application change.
【0020】また、フィルム厚さ方向の吸湿膨張係数に
ついても、0〜600ppm/%RHであるのが好まし
いことが判明した。より好ましくは、0〜500ppm
/%RHである。フィルム厚さ方向の吸湿膨張係数が大
きすぎると、フィルムをロール状に捲いた時の捲姿が悪
くなることがあり、その結果としてフィルムの平坦性の
悪化や加工性の低下をきたす。吸湿膨張係数の低減化
は、ポリマー種の選択、延伸配向度・結晶化度・ポリマ
ー末端基の調整などにより達成できる。It was also found that the coefficient of hygroscopic expansion in the film thickness direction is preferably 0 to 600 ppm /% RH. More preferably, 0 to 500 ppm
/% RH. If the coefficient of hygroscopic expansion in the thickness direction of the film is too large, the rolled form of the film may be poor, resulting in poor flatness and poor workability of the film. The reduction of the coefficient of hygroscopic expansion can be achieved by selecting the type of polymer, adjusting the degree of stretching orientation, the degree of crystallinity, and the polymer end group.
【0021】本発明のフィルムとして、200℃での熱
収縮率が0〜0.5%のものが好ましい。何故なら、熱
収縮が大きいと、フィルムの加工工程等で高温履歴を受
けたとき、フィルムの平坦性などが低下することがある
からである。熱収縮率の低減化は、ポリマー種の選択、
熱セットなどによって達成できる。また、熱収縮率のバ
ラツキが0.1%以下であることが、湿熱処理後のフィ
ルムの一直性や平坦性を良好なレベルに保つ上で望まし
い。熱収縮率のバラツキは、フィルムの任意の場所で測
った10点の最大値と最小値の差で定義される。熱収縮
率のバラツキの低減化は、フィルム製造工程において延
伸、乾燥、熱処理、熱固定の各工程条件の幅方向および
時間変動の抑制が重要である。The film of the present invention preferably has a heat shrinkage at 200 ° C. of 0 to 0.5%. The reason is that if the heat shrinkage is large, the flatness of the film may be reduced when the film is subjected to a high-temperature history in the film processing step or the like. The reduction of the heat shrinkage rate depends on the choice of polymer type,
This can be achieved by heat setting or the like. Further, it is desirable that the variation in the heat shrinkage is not more than 0.1% in order to maintain the uniformity and flatness of the film after the wet heat treatment at a favorable level. The variation in the heat shrinkage is defined by the difference between the maximum value and the minimum value of 10 points measured at an arbitrary position on the film. In order to reduce the variation in the heat shrinkage, it is important to suppress the fluctuation in the width direction and the time in the process conditions of stretching, drying, heat treatment, and heat setting in the film manufacturing process.
【0022】本発明のフィルムは、好ましくは、金属鏡
面との動摩擦係数が0.02〜0.25の範囲にあり、
更に好ましくは0.02〜0.15である。摩擦係数が
小さすぎると加工工程での取扱が不安定になり、逆に大
きすぎると加工工程でのしわ・歪の発生や傷つきが多く
なるからである。摩擦係数の調整は、易滑剤の添加量・
種類・粒度・分散度等の選択によって達成でき、好まし
くは易滑剤を0.01〜3重量%添加する。The film of the present invention preferably has a coefficient of dynamic friction with a metal mirror surface in the range of 0.02 to 0.25,
More preferably, it is 0.02 to 0.15. If the coefficient of friction is too small, handling in the processing step becomes unstable, and if it is too large, wrinkling, distortion and damage are increased in the processing step. Adjustment of friction coefficient depends on the amount of lubricant
This can be achieved by selecting the type, particle size, degree of dispersion, etc., and preferably 0.01 to 3% by weight of a lubricant is added.
【0023】本発明のフィルムは、更に、IEC−11
2に準じて測定した耐トラッキング性(CTI)が、好
ましくは、200〜1000を有している。これは、イ
オン性の環境下に於いても電気絶縁性に優れていること
を示している。本発明のフィルムは、好ましくは、0.
8μm以上の高さの表面粗大突起を実質的に含有しな
い。フィルムのこの特徴は、易滑剤の粒度・分散度の選
択によって達成できる。The film of the present invention further comprises IEC-11
2 has a tracking resistance (CTI) of preferably 200 to 1,000. This indicates that the electrical insulation is excellent even in an ionic environment. The film of the present invention preferably has a thickness of 0.1 mm.
Substantially no surface coarse protrusions having a height of 8 μm or more. This characteristic of the film can be achieved by selecting the particle size and dispersity of the lubricant.
【0024】本発明のフィルムの製造法については、特
に限定されないが、高ヤング率化すること、洗浄抽出可
能な塩素含量を少なくするための特別の手段をとること
を満たして製造する必要がある。アラミドについて、有
機溶剤可溶のものでは、直接溶剤中で重合するか、一旦
ポリマーを単離した後再溶解するなどして溶液とし、つ
いで乾式法または湿式法にて製膜し、また、ポリパラフ
ェニレンテレフタルアミド(PPTA)等の有機溶剤に
難溶のものについては、濃硫酸などに溶解して溶液と
し、ついで乾式法または湿式法にて製膜する。The method of producing the film of the present invention is not particularly limited, but it is necessary to satisfy the requirement of increasing the Young's modulus and taking special measures to reduce the chlorine content which can be extracted by washing. . As for aramid, if it is soluble in an organic solvent, it is polymerized directly in a solvent, or once a polymer is isolated and redissolved to form a solution, and then formed into a film by a dry method or a wet method. Those which are hardly soluble in an organic solvent such as paraphenylene terephthalamide (PPTA) are dissolved in concentrated sulfuric acid or the like to form a solution, and then formed into a film by a dry method or a wet method.
【0025】乾式法では、溶液はダイから押し出し、金
属ドラムやエンドレスベルトなどの支持体上にキャスト
し、キャストした溶液が自己支持性のあるフィルムを形
成するまで溶剤除去を行う。湿式法では、溶液はダイか
ら直接凝固液中に押し出すか、乾式と同様に金属ドラム
またはエンドレスベルト上にキャストした後、凝固液中
で、凝固させる。ポリマー溶液が光学異方性である場合
には、ポリマー溶液を凝固させる前に光学等方性溶液に
変換する必要がある。光学異方性を残したまま凝固させ
ると、得られるフィルムは一方向に裂けやすく、フィル
ムとして用いることが出来ない。光学等方性への変換は
支持体上に流延後に行うのが好ましい。In the dry method, the solution is extruded from a die, cast on a support such as a metal drum or an endless belt, and the solvent is removed until the cast solution forms a self-supporting film. In the wet method, the solution is extruded directly from a die into a coagulating liquid, or cast on a metal drum or an endless belt as in the dry method, and then coagulated in the coagulating liquid. If the polymer solution is optically anisotropic, it needs to be converted to an optically isotropic solution before solidifying the polymer solution. If the film is coagulated with the optical anisotropy remaining, the resulting film tends to tear in one direction and cannot be used as a film. Conversion to optical isotropicity is preferably performed after casting on a support.
【0026】乾式法、湿式法ともに、引き続き、フィル
ム中の溶剤や無機塩などを洗浄し、延伸、乾燥、熱処理
などの処理を行う。本発明のフィルムを得る上で、フィ
ルムの洗浄工程は重要である。アラミドは極性の強いポ
リマーであるため、イオン性化合物や有機極性低分子化
合物が配位しやすく、このため通常の洗浄法では約10
0ppm以下の残存物量にすることが困難であるからで
ある。本発明者の研究では、特別の洗浄法を組合せて初
めて本発明のフィルムが得られた。In both the dry method and the wet method, a solvent, an inorganic salt, and the like in the film are washed, and a process such as stretching, drying, and heat treatment is performed. In obtaining the film of the present invention, the film washing step is important. Since aramid is a highly polar polymer, ionic compounds and low-molecular organic polar compounds are easily coordinated.
This is because it is difficult to reduce the residual amount to 0 ppm or less. In the study of the present inventors, the film of the present invention was obtained only by combining a special washing method.
【0027】即ち、重合副生物としての塩化水素が残存
しているとき、または/及び溶媒として硫酸などの酸を
使用したとき、アルカリでの中和を当量よりも過剰にす
ることが先ず大事である。また、洗浄により約1000
ppm以下の残存溶媒量になった後、50℃以上の熱水
で洗浄すること及び超音波付与しながら洗浄することに
より、溶媒、塩、アルカリなどの残存物量を徹底して少
なくすることが必要である。ただし、上記方法以外の方
法を排除するものではない。That is, when hydrogen chloride as a by-product of the polymerization remains or / and when an acid such as sulfuric acid is used as a solvent, it is important to first make the neutralization with an alkali in excess of the equivalent amount. is there. In addition, about 1000
After the residual solvent amount becomes less than ppm, it is necessary to thoroughly reduce the residual amount of solvent, salt, alkali, etc. by washing with hot water of 50 ° C. or more and washing while applying ultrasonic waves. It is. However, a method other than the above method is not excluded.
【0028】洗浄を完了させた後、フィルムを湿潤延伸
する。本発明のフィルムのヤング率を確保するために
は、何れの製膜方法に於いても、面積延伸倍率を0.9
〜5.0倍にするのが好ましく、より好ましくは、1.
0〜4.0倍である。0.9未満の面積延伸倍率では、
ヤング率が不十分になる。フィルムの密度バラツキを小
さくし、湿熱処理後のフィルムの平坦性、一直性を良好
にするために、延伸速度を約50%/秒以下にするのが
好ましい。After the washing is completed, the film is wet-drawn. In order to secure the Young's modulus of the film of the present invention, in any of the film forming methods, the area stretching ratio is 0.9.
It is preferably set to be up to 5.0 times, more preferably 1.
It is 0 to 4.0 times. At an area stretch ratio of less than 0.9,
The Young's modulus becomes insufficient. In order to reduce the variation in the density of the film and to improve the flatness and uniformity of the film after the wet heat treatment, the stretching speed is preferably set to about 50% / second or less.
【0029】乾燥、熱処理は、一般的に100〜600
℃の加熱条件下に行われる。これらのうち、乾燥と熱処
理を分けて行うのが好ましい。フィルムを乾燥させる場
合、あまり急激に加熱するとフィルム内にボイドが生
じ、表面平滑性の低下や破断伸度の低下を結果し、フィ
ルムの密度バラツキの増大による平坦性、一直性の低下
をもたらすことがあるため、100〜300℃、特に1
50〜250℃の加熱条件下に行うのが好ましい。フィ
ルムの熱処理はヤング率、熱寸法安定性を向上させる目
的で、300〜550℃で実施するのが好ましい。熱処
理法として、接触式、非接触式いずれを用いてもよく、
例えば温度コントロールしたロールに接触させる方法、
赤外線加熱、板状ヒータ間で非接触で加熱する方法など
がある。Drying and heat treatment are generally performed at 100 to 600
It is performed under heating conditions of ° C. Of these, drying and heat treatment are preferably performed separately. When the film is dried, if it is heated too rapidly, voids are formed in the film, resulting in a decrease in surface smoothness and a decrease in elongation at break, resulting in a decrease in flatness and linearity due to an increase in density variation of the film. 100-300 ° C, especially 1
It is preferable to carry out under heating conditions of 50 to 250 ° C. The heat treatment of the film is preferably performed at 300 to 550 ° C. for the purpose of improving Young's modulus and thermal dimensional stability. As the heat treatment method, any of a contact type and a non-contact type may be used,
For example, a method of contacting a roll with temperature control,
Infrared heating, a method of heating in a non-contact manner between plate heaters, and the like are available.
【0030】本発明のフィルムは、フィルム表面と他の
材料との親和性、接着性を改良するために、フィルム表
面に改質処理を行っても良い。表面改質処理としては、
コロナ放電処理、プラズマ処理などが知られている。フ
ィルム同志の滑り性を良くしたり、ブロッキング現象を
防ぐため、フィルムに微粒子を混在させる方法が、通常
とられ、この微粒子を易滑剤とも称する。微粒子として
は、有機化合物、無機化合物があるが、通常は、例えば
SiO2、TiO2、ZnO、Al2O3、CaSO4、B
aSO4、CaCO3、カーボンブラック、ゼオライト、
その他金属粉末などの無機化合物が用いられるが、重要
なことは塩素化合物を実質的に含有しないことであ
る。。粒子径は0.01〜2μm、添加量は0.03〜
5重量%に選ばれることが多い。即ち、アラミドの溶液
中に、上記微粒子を混入し、この溶液を製膜することに
より製造される。この際、微粒子の分散を良くするため
に、超音波方式や撹拌方式のホモジナイザーが好ましく
用いられる。The film of the present invention may be subjected to a modification treatment on the film surface in order to improve the affinity and adhesion between the film surface and other materials. As the surface modification treatment,
Corona discharge treatment, plasma treatment and the like are known. In order to improve the slipperiness of the films or to prevent the blocking phenomenon, a method of mixing fine particles into the film is usually employed, and the fine particles are also referred to as a lubricant. The fine particles include organic compounds and inorganic compounds. Usually, for example, SiO 2 , TiO 2 , ZnO, Al 2 O 3 , CaSO 4 , B
aSO 4 , CaCO 3 , carbon black, zeolite,
Other inorganic compounds such as metal powders are used, but what is important is that they contain substantially no chlorine compounds. . The particle size is 0.01 to 2 μm, and the amount added is 0.03 to
It is often chosen as 5% by weight. That is, it is produced by mixing the fine particles in an aramid solution and forming a film of the solution. At this time, in order to improve the dispersion of the fine particles, a homogenizer of an ultrasonic system or a stirring system is preferably used.
【0031】[0031]
【発明の実施の形態】以下、実施例により本発明をより
具体的に説明する。なお、実施例における特性値の測定
法は次の通りである。 (1)フィルムの厚み、強度、伸度、ヤング率の測定法 フィルムの厚みは、直径2mmの測定面を持つダイヤル
ゲージで測定する。DESCRIPTION OF THE PREFERRED EMBODIMENTS Hereinafter, the present invention will be described in more detail with reference to examples. In addition, the measuring method of the characteristic value in an Example is as follows. (1) Method of measuring film thickness, strength, elongation and Young's modulus The film thickness is measured with a dial gauge having a measurement surface of 2 mm in diameter.
【0032】強度、伸度、ヤング率は、定速伸長型強伸
度測定機を用い、測定長100mm、引張速度50mm
/分で測定したもので、フィルムの長手方向とその直角
方向との平均値で表した。 (2)熱収縮率の測定法 フィルムから2cm×5cmの試料片を切り出し、この
試験片の一端から5mm、45mmの箇所に刃物で傷を
つけて標識とし、予め23℃、55%RHの雰囲気下に
72時間放置した後、標識間の距離(L0 )を「読み取
り顕微鏡」にて測定し、次いで200℃の熱風式オーブ
ンに2時間拘束することなく放置した後、再度23℃、
55%RHの雰囲気下に72時間放置した後、標識間の
距離(L 1 )を「読み取り顕微鏡」にて測定して、熱収
縮率(%)={(L0 −L1 )/L1 }×100を求め
た。熱収縮率のバラツキは、フィルムから任意にサンプ
リングした10点の試料についての最大値と最小値の差
で示した。The strength, elongation and Young's modulus are constant-speed elongation
Using a measuring machine, measuring length 100mm, pulling speed 50mm
/ Min, measured in the longitudinal direction of the film and its right angle
Expressed as the average value with the direction. (2) Method of measuring heat shrinkage A 2 cm × 5 cm sample piece was cut out from a film and
Scratches 5mm and 45mm from one end of the test piece with a blade
Attach it as a label and put it in advance in an atmosphere of 23 ° C. and 55% RH.
After standing for 72 hours, the distance between the signs (L0)
And a hot-air oven at 200 ° C
And left at 23 ° C.
After leaving for 72 hours in an atmosphere of 55% RH,
Distance (L 1) Is measured with a “reading microscope”
Shrinkage (%) = {(L0-L1) / L1} × 100
Was. Variations in heat shrinkage can be arbitrarily sampled from the film.
Difference between maximum and minimum values for 10 ringed samples
Indicated by
【0033】(3)洗浄抽出される塩素量の測定法 フィルムを細断し、ソックスレー抽出器に入れてイオン
交換水にて3時間ソックスレー抽出し、抽出液をDIO
NEX社製のイオンクロマトグラフィで定量した。 (4)フィルム面方向の吸湿膨張係数の測定法 熱力学特性測定機(TMA、真空理工株式会社製TM7
000型)に幅5mmのサンプルを取り付け、荷重0.
3g下で、一旦300℃まで昇温した後、乾燥窒素気流
下により冷却し、23℃における乾燥窒素と空気との間
の湿度変化、及びフィルムの寸法変化を測定し、下記式
により計算し、求めた。(3) Method for measuring the amount of chlorine extracted by washing The film was cut into pieces, placed in a Soxhlet extractor, and subjected to Soxhlet extraction with ion-exchanged water for 3 hours.
It was quantified by ion chromatography manufactured by NEX. (4) Method for measuring coefficient of hygroscopic expansion in the film surface direction Thermodynamic property measuring instrument (TMA, TM7 manufactured by Vacuum Riko Co., Ltd.)
000 type), a sample with a width of 5 mm was attached, and a load of 0.
Under 3 g, the temperature was once raised to 300 ° C., then cooled under a dry nitrogen stream, the humidity change between dry nitrogen and air at 23 ° C., and the dimensional change of the film were measured and calculated by the following formula, I asked.
【0034】 〔(FA −FN )/FN 〕×〔1/(MA −MN )〕 但し、FA =空気中のフイルムの寸法 FN =乾燥窒素中のフイルムの寸法 MA =空気の湿度 MN =乾燥窒素の湿度 (5)耐トラッキング性(CTI値)の測定法 IEC−112に準じて、予め段階的に電圧を印加した
フィルムにNH4Cl水溶液を滴下し、トラッキング破
壊を示す滴下数が50以上になる最大の印加電圧を求
め、CTI値とした。[(F A −F N ) / F N ] × [1 / (M A −M N )] where F A = dimension of film in air F N = dimension of film in dry nitrogen M A = Humidity of air M N = Humidity of dry nitrogen (5) Measurement method of tracking resistance (CTI value) According to IEC-112, a NH 4 Cl aqueous solution is dropped on a film to which voltage is applied stepwise in advance, and tracking is performed. The maximum applied voltage at which the number of drops indicating destruction became 50 or more was determined and defined as the CTI value.
【0035】(6)耐湿熱性の測定法 湿熱処理として、フィルムを50℃、80%RHの雰囲
気に7日間静置し、その前後でのフィルム特性の比較を
行った。 (7)接着力の測定法 コロナ放電処理したフィルムを150℃で3分間乾燥し
た後、35μm厚みの銅箔と接着剤(スリーボンド社製
TB1650)を使用して銅張積層板を作成し、100
℃で2時間、ついで150℃で3時間硬化させた。この
試料を幅1cmに切断し、引張試験機にて引張速度50
mm/分で180度剥離をおこない、その抵抗力を接着
力とした。(6) Method of Measuring Moisture Heat Resistance As a wet heat treatment, the film was allowed to stand in an atmosphere of 50 ° C. and 80% RH for 7 days, and the film characteristics before and after that were compared. (7) Method of measuring adhesive strength A film subjected to corona discharge treatment was dried at 150 ° C. for 3 minutes, and then a copper-clad laminate was prepared using a copper foil having a thickness of 35 μm and an adhesive (TB1650 manufactured by Three Bond Co.)
Cured for 2 hours at 150C and then for 3 hours at 150C. This sample was cut to a width of 1 cm, and a tensile tester was used to obtain a tensile speed of 50 cm.
Peeling was performed at 180 ° at mm / min, and the resistance was defined as the adhesive strength.
【0036】(8)平坦性の評価 フィルムを水平面上に展開し手で軽く張力をかけたとき
のフィルムの平坦性で相対比較して、全く問題ないもの
を○、少し波打っているものを△、波打ちの大きいもの
を×、で表した。 (9)一直性の測定法 長手方向に1mの長さのフイルムを採取し、これを水平
面上に置き、フイルムの湾曲によって生じる長手方向の
隣り合う湾曲頂点間を結ぶ線分をひき、この線分が湾曲
内側の弧と乖離する最大の距離を測る。これを全ての隣
り合う頂点間で行い、その最大値をフイルムの湾曲量と
した。フイルムの一直性は湾曲量の少なさで表される。(8) Evaluation of flatness When the film was spread on a horizontal surface and lightly tensioned by hand, the film was compared with the flatness relative to the film. △, those with large undulations were represented by ×. (9) Method of measuring linearity A film having a length of 1 m is sampled in the longitudinal direction, placed on a horizontal plane, and a line segment between adjacent curved vertexes in the longitudinal direction caused by the curvature of the film is drawn. Measure the maximum distance that the minute deviates from the arc inside the curve. This was performed between all adjacent vertices, and the maximum value was defined as the amount of film bending. The intuition of the film is represented by a small amount of bending.
【0037】[0037]
【比較例1】特開昭63−141207号公報の実施例
1を追試した。ポリバラフェニレンテレフタルアミド
(PPTA)を99.1%の硫酸にポリマー濃度12.
5%で溶解し、70℃で光学異方性をもつドープを得、
5時間かけて真空脱気した。70℃に保ったドープを
0.6mmのスリットを有するダイから3.5m/分の
吐出線速度で鏡面に磨いたタンタル製のエンドレスベル
ト上にキャストし、相対湿度85%90℃の空気を吹き
付けて、流延ドープを光学等方化し、ベルトと共に、−
5℃の30%硫酸水溶液の中に導いて凝固させた。Comparative Example 1 Example 1 of JP-A-63-141207 was additionally tested. 11. Polybaraphenylene terephthalamide (PPTA) in 99.1% sulfuric acid with a polymer concentration of 12.
Dissolved at 5% to obtain a dope having optical anisotropy at 70 ° C.
Vacuum degassed for 5 hours. The dope kept at 70 ° C. was cast from a die having a slit of 0.6 mm at an ejection linear speed of 3.5 m / min onto an endless belt made of mirror-polished tantalum, and blown with air at 85% relative humidity and 90 ° C. Then, the casting dope is made optically isotropic and, together with the belt,
The solution was introduced into a 30% aqueous sulfuric acid solution at 5 ° C. for coagulation.
【0038】ついで、凝固フィルムをベルトから引き剥
がし、40℃温水中を走行させて洗浄した。洗浄を終了
したフィルムをテンターに導き、フィルムの走行方向及
びそれと直角な方向ともに90%に収縮させながら15
0℃の熱風で乾燥し、テンターの出口で280℃の熱板
に接触させて熱処理した。このようにして得られたフィ
ルムをフィルムAとして、その性質を表1に示した。Next, the coagulated film was peeled off from the belt and washed by running in hot water at 40 ° C. The washed film is guided to a tenter and shrunk to 90% in both the running direction of the film and the direction perpendicular to the running direction.
It was dried with hot air at 0 ° C., and was heat-treated by contacting with a hot plate at 280 ° C. at the exit of the tenter. The film thus obtained was designated as Film A, and the properties thereof are shown in Table 1.
【0039】次に、ダイのスリットを0.8mmにし
て、かつ乾燥を1.05倍の延伸下に行って得たフィル
ムをフィルムBとして、その性質を表1に示した。Next, the properties of the film obtained by setting the slit of the die to 0.8 mm and performing drying under stretching of 1.05 times as Film B are shown in Table 1.
【0040】[0040]
【実施例1】PPTAを、99.8%硫酸に、ポリマー
濃度が12%になるように溶解し、0.3mmのスリッ
ト間隔のダイからエンドレスベルト上にキャストした。
硫酸には、予め0.04μmのシリカ粒子をPPTAに
対し0.3重量%となるように超音波撹拌機により分散
させておいた。ベルト上で加熱と同時に吸湿処理して、
ドープを液晶相から等方相に相転換した後、0℃の45
%硫酸中にて凝固させた。凝固浴から引き出したフィル
ムを苛性ソーダ水溶液に浸漬して、PHが約8になるま
で過剰に中和し、ついでこれを水洗してPH7.0〜
7.1にした後、60℃の熱水中で超音波をかけながら
更に洗浄を行った。Example 1 PPTA was dissolved in 99.8% sulfuric acid so as to have a polymer concentration of 12%, and cast on an endless belt from a die having a slit interval of 0.3 mm.
In the sulfuric acid, 0.04 μm silica particles were previously dispersed by an ultrasonic stirrer so as to be 0.3% by weight with respect to PPTA. Moisture absorption treatment at the same time as heating on the belt,
After inverting the dope from the liquid crystal phase to the isotropic phase, 45 ° C.
Coagulated in 5% sulfuric acid. The film drawn from the coagulation bath is immersed in an aqueous solution of caustic soda to neutralize excessively until the pH becomes about 8, and then washed with water to obtain a pH of 7.0 to 7.0.
After being adjusted to 7.1, washing was further performed while applying ultrasonic waves in hot water at 60 ° C.
【0041】つぎに、湿潤フィルムを長さ方向に1.1
倍延伸した後クリップテンターにより1.1倍に横延伸
し、ついで定長状態を保ちつつ150℃で熱風乾燥し、
400℃で緊張熱処理し、300℃でフリー熱処理した
後、捲き上げた。ここで、延伸速度を縦横ともに約20
%/秒で行い、横延伸及び乾燥時にフィルムの幅方向に
5℃以上の温度むらが生じないように、テンターのクリ
ップの冷却及び加熱を特別に付加した装置で充分に行
い、また緊張熱処理のヒータの温度分布も中央部と端部
とで5℃以上の差が出ないように、端部の放熱を防止す
べく保温を付加した。Next, the wet film is moved in the longitudinal direction by 1.1.
After stretching twice, it was stretched transversely to 1.1 times by a clip tenter, and then dried with hot air at 150 ° C. while maintaining a constant length state.
After a tension heat treatment at 400 ° C. and a free heat treatment at 300 ° C., it was rolled up. Here, the stretching speed is about 20
% / Sec. In order to prevent temperature unevenness of 5 ° C. or more from occurring in the width direction of the film during transverse stretching and drying, the cooling and heating of the tenter clip are sufficiently performed with a specially added device. In order to prevent the temperature distribution of the heater from having a difference of 5 ° C. or more between the center portion and the end portion, heat retention was added to prevent heat radiation at the end portion.
【0042】幅500mm、長さ300mで得られたP
PTAフィルムは25μmの平均厚みであり、長尺方
向、幅方向に物性差は殆ど無く、表1に示す通りだっ
た。比較例1のフィルムに比べ、洗浄抽出される塩素量
が著しく少なく、湿熱処理によるフィルム特性の低下が
殆どなかった。P obtained in a width of 500 mm and a length of 300 m
The PTA film had an average thickness of 25 μm, and there was almost no difference in physical properties in the longitudinal direction and the width direction, as shown in Table 1. Compared to the film of Comparative Example 1, the amount of chlorine extracted and washed was significantly smaller, and the film properties were not substantially reduced by the wet heat treatment.
【0043】[0043]
【表1】 [Table 1]
【0044】[0044]
【実施例2】実施例1において、ダイのスリット間隔を
0.1mmにし、延伸率を縦横ともに1.2にし、延伸
速度を約35%/秒に変えた以外は、実施例1と同一と
した。得られたフィルムの物性は縦横バランスしてお
り、表2に示す通りで、洗浄抽出される塩素量が極度に
少なく、耐湿熱性は全く問題なかった。Example 2 Example 1 was the same as Example 1 except that the slit interval of the die was 0.1 mm, the stretching ratio was 1.2 in both length and width, and the stretching speed was changed to about 35% / sec. did. The physical properties of the obtained film were balanced vertically and horizontally, and as shown in Table 2, the amount of chlorine extracted and washed was extremely small, and there was no problem with the heat and humidity resistance.
【0045】[0045]
【比較例2】実施例2において、苛性ソーダによる中和
及び超音波照射を取りやめ、室温の水による洗浄をPH
6.9以上になるように徹底して行い、それら以外は実
施例2と同一に行った。得られたフィルムの物性は表2
に示す通りで、湿熱処理で伸度、接着力、一直性等がか
なり低下した。Comparative Example 2 In Example 2, neutralization with caustic soda and irradiation with ultrasonic waves were stopped, and washing with water at room temperature was carried out.
Thoroughly performed so as to be 6.9 or more, and the other steps were the same as in Example 2. Table 2 shows the physical properties of the obtained film.
As shown in the figure, elongation, adhesive strength, straightness, etc. were considerably reduced by the wet heat treatment.
【0046】[0046]
【実施例3】ポリパラフェニレン−2−クロロテレフタ
ルアミド(PPClTA)をポリマー濃度が13重量%
になるように溶解し、約0.4mmのスリット間隔のダ
イからエンドレスベルト上にキャストした。濃硫酸に
は、予め0.02μmの酸化チタン微粒子をPPClT
Aに対し0.2重量%となるように超音波分散機により
分散させておいた。実施例1と同様の操作を加え、フィ
ルムをつくった。EXAMPLE 3 Polyparaphenylene-2-chloroterephthalamide (PPClTA) was added at a polymer concentration of 13% by weight.
And cast on an endless belt from a die with a slit spacing of about 0.4 mm. For concentrated sulfuric acid, fine titanium oxide particles of 0.02 μm
A was dispersed by an ultrasonic dispersing machine so that the content of A was 0.2% by weight. The same operation as in Example 1 was performed to prepare a film.
【0047】縦横の物性のバランスしたフィルムが得ら
れ、それを表2に示した。A film having balanced properties in the vertical and horizontal directions was obtained, and is shown in Table 2.
【0048】[0048]
【表2】 [Table 2]
【0049】[0049]
【発明の効果】本発明によれば、湿熱処理を受けても性
能低下のないアラミドフィルムが得られる。即ち、従来
のアラミドフィルムは、湿熱処理により、強伸度等の機
械的性質、電気絶縁性、接着力等が低下するだけでな
く、フィルムの平坦性や一直性が低下して、フィルムの
加工性が劣るようになったが、本発明のフィルムではこ
のような欠点が解消されている。According to the present invention, it is possible to obtain an aramid film having no performance deterioration even when subjected to a wet heat treatment. That is, the conventional aramid film not only deteriorates mechanical properties such as high elongation, electric insulation, adhesive strength, etc., but also reduces flatness and straightness of the film due to wet heat treatment. However, the film of the present invention has eliminated such disadvantages.
【0050】このため、本発明のフィルムを、磁気テー
プのベースフィルム、プリンター用インクシート、太陽
電池基板、フレキシブルプリント配線板用ベースフィル
ム、音響材、電気絶縁材等に使用したとき、高温多湿の
過酷な使用環境においても、材料としての信頼性が従来
のアラミドフィルムより一段優れており、アラミドフィ
ルムの持つ本来の性質、例えば高い耐熱性、高ヤング
率、良好な寸法安定性と相まって、これらの用途に極め
て有用である。Therefore, when the film of the present invention is used for a base film of a magnetic tape, an ink sheet for a printer, a solar cell substrate, a base film for a flexible printed wiring board, an acoustic material, an electric insulating material, etc. Even in harsh usage environments, the reliability as a material is far superior to conventional aramid films, and coupled with the inherent properties of aramid films, such as high heat resistance, high Young's modulus, and good dimensional stability, Very useful for applications.
Claims (1)
2のアラミドフィルムにおいて、洗浄抽出される塩素量
が0.001〜8ppmであることを特徴とする高剛性
耐熱アラミドフィルム。1. A Young's modulus of 700 to 2500 kg / mm
2. The high-rigidity heat-resistant aramid film according to 2 , wherein the amount of chlorine extracted by washing is 0.001 to 8 ppm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21082097A JPH1149876A (en) | 1997-08-05 | 1997-08-05 | Highly rigid heat-resistant aramide film |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP21082097A JPH1149876A (en) | 1997-08-05 | 1997-08-05 | Highly rigid heat-resistant aramide film |
Publications (1)
Publication Number | Publication Date |
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JPH1149876A true JPH1149876A (en) | 1999-02-23 |
Family
ID=16595671
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JP21082097A Pending JPH1149876A (en) | 1997-08-05 | 1997-08-05 | Highly rigid heat-resistant aramide film |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004039863A1 (en) * | 2002-10-31 | 2004-05-13 | Toray Industries, Inc. | Alicyclic or aromatic polyamides, polyamide films, optical members made by using the same, and polyamide copolymers |
JP2007284802A (en) * | 2006-04-12 | 2007-11-01 | Teijin Techno Products Ltd | Heat-resistant protective wear |
JP2009256610A (en) * | 2008-03-28 | 2009-11-05 | Toray Ind Inc | Aromatic polyamide and method for producing the same |
CN103194058A (en) * | 2013-04-08 | 2013-07-10 | 桂林电子科技大学 | High-thermal-conductive moisture permeable film and preparation method thereof |
JP2014001313A (en) * | 2012-06-18 | 2014-01-09 | Asahi Kasei Chemicals Corp | Polyamide, and molded article thereof |
-
1997
- 1997-08-05 JP JP21082097A patent/JPH1149876A/en active Pending
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2004039863A1 (en) * | 2002-10-31 | 2004-05-13 | Toray Industries, Inc. | Alicyclic or aromatic polyamides, polyamide films, optical members made by using the same, and polyamide copolymers |
JPWO2004039863A1 (en) * | 2002-10-31 | 2006-03-02 | 東レ株式会社 | Cycloaliphatic or aromatic polyamide, polyamide film, optical member using them, and polyamide copolymer |
CN100343308C (en) * | 2002-10-31 | 2007-10-17 | 东丽株式会社 | Alicyclic or aromatic polyamides, polyamide films, optical members made by using the same, and polyamide copolymers |
US8153753B2 (en) | 2002-10-31 | 2012-04-10 | Toray Industries, Inc. | Alicyclic or aromatic polyamides, polyamide films, optical members made by using the same, and polyamide copolymers |
JP4945898B2 (en) * | 2002-10-31 | 2012-06-06 | 東レ株式会社 | Polyamide film and optical member using the same |
JP2007284802A (en) * | 2006-04-12 | 2007-11-01 | Teijin Techno Products Ltd | Heat-resistant protective wear |
JP2009256610A (en) * | 2008-03-28 | 2009-11-05 | Toray Ind Inc | Aromatic polyamide and method for producing the same |
JP2014001313A (en) * | 2012-06-18 | 2014-01-09 | Asahi Kasei Chemicals Corp | Polyamide, and molded article thereof |
CN103194058A (en) * | 2013-04-08 | 2013-07-10 | 桂林电子科技大学 | High-thermal-conductive moisture permeable film and preparation method thereof |
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