JPH0637562B2 - Polymer composite manufacturing method - Google Patents
Polymer composite manufacturing methodInfo
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- JPH0637562B2 JPH0637562B2 JP14329087A JP14329087A JPH0637562B2 JP H0637562 B2 JPH0637562 B2 JP H0637562B2 JP 14329087 A JP14329087 A JP 14329087A JP 14329087 A JP14329087 A JP 14329087A JP H0637562 B2 JPH0637562 B2 JP H0637562B2
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Description
【発明の詳細な説明】 〈技術分野〉 繊維強化プラスチックは、飛躍的に向上した物性の故に
耐荷重構造用材料として重要視され各種各様の材料が開
発され、実用化されてきた。かかる複合材料の製造に
は、別途製造された強化用繊維を一方向に並べる工程
や、更にマトリックスを含浸させる工程を要し、しかも
その際オートクレーブ中で行う工程が入る等の複雑な段
階的操作を必要とする。DETAILED DESCRIPTION OF THE INVENTION Technical Field Fiber-reinforced plastics are regarded as important as load-bearing structural materials because of their dramatically improved physical properties, and various kinds of materials have been developed and put into practical use. The production of such a composite material requires a step of arranging separately produced reinforcing fibers in one direction and a step of further impregnating a matrix, and at that time, a complicated stepwise operation such as a step performed in an autoclave is included. Need.
一方複合材料の強度と耐久度は、強化用繊維とマトリッ
クス高分子との界面の状態に大きく左右される。両者の
界面は繊維自体がマクロなため、そこに存在する欠陥は
マクロに伝播し、複合材料の破壊につながる。On the other hand, the strength and durability of the composite material largely depend on the state of the interface between the reinforcing fiber and the matrix polymer. Since the fiber itself is a macro at the interface between the two, defects existing there propagate to the macro, leading to the destruction of the composite material.
かかる欠点を解決するために、マクロな形状でしか分散
しえない繊維状強化材に代えて、高モジュラスの補強用
高分子とマトリックス高分子とを共通溶媒中に溶解し
て、両者をミクロな分子的オーダで混合しこれを凝固・
成形することにより、補強用高分子が極めてミクロな状
態で分散,混合し、しかも補強用高分子が配向してなる
高分子複合体を製造することが検討されてきた。In order to solve such a drawback, in place of the fibrous reinforcing material that can be dispersed only in a macro shape, a high modulus reinforcing polymer and a matrix polymer are dissolved in a common solvent, and both are micro-dispersed. Mix by molecular order and solidify /
It has been studied to produce a polymer composite in which the reinforcing polymer is dispersed and mixed in an extremely microscopic state by molding and the reinforcing polymer is oriented.
本発明者らは、現在有機高分子繊維として、優れた引張
りモジュラスを与えるポリ−p−フェニレンベンゾビス
チアゾール等のポリアゾール系高分子を補強用高分子と
して用い、各種マトリックスポリマーとの各組合せ系で
の高モジュラス化について検討を進めてきたが、両高分
子成分が十分に配向した時に期待される加成性値に比べ
て例えば引張りモジュラスが低い等の欠点があった。ま
た、高分子複合体のフイルムを積層した成形物を得るた
めには、該フイルムの厚さを厚くした方が成形上有利で
あるが、従来の湿式成形では厚さを厚くすると凝固性が
悪化し、良好なフイルムが得られなかった。The present inventors have now used, as an organic polymer fiber, a polyazole-based polymer such as poly-p-phenylenebenzobisthiazole, which gives an excellent tensile modulus, as a reinforcing polymer, and in each combination system with various matrix polymers. However, there was a defect that the tensile modulus was lower than the expected additivity value when both polymer components were sufficiently oriented. Further, in order to obtain a molded product in which a film of a polymer composite is laminated, it is advantageous in terms of molding to increase the thickness of the film, but in conventional wet molding, increasing the thickness deteriorates coagulation properties. However, a good film could not be obtained.
本発明者らは、かかる問題点を解決すべくポリ−p−フ
ェニレンベンゾビスチアゾール等のポリアゾール系高分
子を補強用高分子として用い、マトリックス高分子とし
て屈曲性高分子を用いた系での高モジュラス化及び厚膜
化について鋭意検討した結果、本発明に到達したもので
ある。In order to solve such a problem, the present inventors have used a polyazole-based polymer such as poly-p-phenylene benzobisthiazole as a reinforcing polymer and a flexible polymer as a matrix polymer. The present invention has been achieved as a result of intensive studies on the modulus and the film thickness.
即ち、本発明は実質的に棒状骨格を有するポリアゾール
からなる補強用高分子(A)と融着性を有するマトリッ
クス高分子(B)とを主として含有する高分子溶液を、
基板上に流延し、次いで凝固浴中に導入して製膜するこ
とからなる高分子複合体の製造法において、当該高分子
溶液が光学的等方性を示す温度領域と、光学的異方性を
示す温度領域とを有し、基板上に流延する際の当該高分
子溶液の温度は光学的異方性を示す温度領域内にあり、
流延後当該高分子溶液を加熱することで見掛け状光学的
等方性を転移せしめつつ凝固浴中に導入することを特徴
とする高分子複合体の製造法である。That is, the present invention provides a polymer solution mainly containing a reinforcing polymer (A) substantially made of polyazole having a rod-like skeleton and a matrix polymer (B) having a fusion property,
In a method for producing a polymer composite, which comprises casting on a substrate and then introducing it into a coagulation bath to form a film, a temperature range in which the polymer solution exhibits optical isotropy and an optical anisotropy are exhibited. And a temperature range exhibiting a property, the temperature of the polymer solution when cast on a substrate is within a temperature range exhibiting optical anisotropy,
After the casting, the polymer solution is introduced into the coagulating bath while transferring the apparent optical isotropy by heating the polymer solution.
本発明において用いる補強用高分子(A)としては、下
記式 [但し、式中Xは−S−,−O−又は−N−を表わし、
結合手(イ),(ロ)は、更にアゾール環又は炭化水素環を形
成する結合手であるか、或いはその一方に水素原子が結
合し、他方が結合手であるものである。] で表わされるアゾール骨格を有する実質的に棒状骨格の
ポリアゾールが挙げられ、具体的には、米国特許第4,20
7,407号明細書に記載されたポリマーがあり、就中ポリ
−p−フェニレンベンゾビスチアゾール,ポリ−p−フ
ェニレンベンゾオキサゾール,ポリ−p−フェニレンベ
ンゾビスイミダゾール等のポリアゾール類が挙げられ
る。The reinforcing polymer (A) used in the present invention has the following formula [Wherein, X represents -S-, -O- or -N-,
The bonds (a) and (b) are bonds that further form an azole ring or a hydrocarbon ring, or a hydrogen atom is bonded to one of them and the other is a bond. ] A substantially rod-like skeleton polyazole having an azole skeleton represented by
There are polymers described in 7,407, among which polyazoles such as poly-p-phenylenebenzobisthiazole, poly-p-phenylenebenzoxazole, and poly-p-phenylenebenzobisimidazole.
補強用高分子(A)の分子量は通常分子量の目安となる
固有粘度が1以上であり、好ましくは1.5以上、特に好
ましくは2以上である。一方、固有粘度が高すぎるもの
は好ましくなく、30になると良好なものが得られない。
本発明の効果を発現するためには補強用高分子の固有粘
度は25以下が好ましく特に好ましくは20以下にするのが
よい。Regarding the molecular weight of the reinforcing polymer (A), the intrinsic viscosity which is a standard of the molecular weight is usually 1 or more, preferably 1.5 or more, particularly preferably 2 or more. On the other hand, those having an intrinsic viscosity that is too high are not preferable, and when the intrinsic viscosity is 30, good ones cannot be obtained.
In order to exert the effects of the present invention, the intrinsic viscosity of the reinforcing polymer is preferably 25 or less, particularly preferably 20 or less.
本発明において用いられるマトリックス高分子(B)
は、補強用高分子(A)と同一溶媒に溶解するものであ
り、ナイロン6,ナイロン66,ナイロン610,ナイロン1
2,ナイロン11等脂肪族ポリアミド;ポリヘキサメチレ
ンイソフタルアミド等の半芳香族ポリアミド;ポリメタ
フェニレンイソフタルアミド等の芳香族ポリアミド;エ
ーテル基等の屈曲性基を導入し屈曲性芳香族ポリアミ
ド;ポリエステル;ポリカーボネート;ポリ酢酸ビニ
ル;ポリサルフォン;ポリエーテルサルフォン;ポリエ
ーテルイミド;ポリエーテルケトン;ポリフェニレンサ
ルファイド等があげられる。Matrix polymer (B) used in the present invention
Is a solvent that dissolves in the same solvent as the reinforcing polymer (A). Nylon 6, nylon 66, nylon 610, nylon 1
2, Nylon 11, etc. Aliphatic polyamides; Semi-aromatic polyamides such as polyhexamethylene isophthalamide; Aromatic polyamides such as polymetaphenylene isophthalamide; Flexible aromatic polyamides by introducing flexible groups such as ether groups; Polyesters; Polycarbonate; polyvinyl acetate; polysulfone; polyether sulfone; polyetherimide; polyether ketone; polyphenylene sulfide and the like.
共通溶媒としては、構成ポリマーを溶解するものであれ
ばよく、例えば濃硫酸,メタンスルホン酸,クロルスル
ホン酸,ポリリン酸,トリフロロ酢酸、リン酸等の酸性
溶媒が挙げられる。これらは適宜混合して用いても良
い。また溶解した高分子の加水分解を押えるため、溶媒
中の水の量をできるだけ少くするための添加剤を混入し
てもよい。例えば発煙硫酸,クロルスルホン酸等の添加
があげられる。The common solvent only needs to dissolve the constituent polymers, and examples thereof include acidic solvents such as concentrated sulfuric acid, methanesulfonic acid, chlorosulfonic acid, polyphosphoric acid, trifluoroacetic acid, phosphoric acid and the like. These may be appropriately mixed and used. Further, in order to suppress the hydrolysis of the dissolved polymer, an additive for reducing the amount of water in the solvent as much as possible may be mixed. Examples include addition of fuming sulfuric acid and chlorosulfonic acid.
高分子複合体形成用の原液は、上記共通溶媒に補強用高
分子とマトリックス高分子とを溶解した高分子溶液であ
り、該高分子溶液は、光学的等方性を示す温度領域と、
光学的異方性を示す温度領域が必要である。The stock solution for forming a polymer complex is a polymer solution in which a reinforcing polymer and a matrix polymer are dissolved in the common solvent, and the polymer solution has a temperature range showing optical isotropy,
A temperature range showing optical anisotropy is required.
光学的等方性を示す温度領域と光学的異方性を示す温度
領域は、ポリマーの種類,重合度,成分比及び濃度によ
って変化するものであるが、以下の測定方法により決定
することができる。The temperature range showing optical isotropy and the temperature range showing optical anisotropy change depending on the type of the polymer, the degree of polymerization, the component ratio and the concentration, and can be determined by the following measuring methods. .
即ち、所定の高分子溶液を調製し、それをスライドガラ
ス上に薄くのばして配置し、高分子溶液の厚さが0.1mm
になるようにしてプレパラートでおさえる。かくして調
製されたサンプルを直交ニコルを有する偏光顕微鏡の観
察下におく。先ずサンプルの温度を室温(20℃)以下に
下げて、スライドガラス上の高分子複合体溶液を光学的
異方性を示す状態とする。That is, prepare a predetermined polymer solution, spread it thinly on a slide glass and arrange it, and the thickness of the polymer solution is 0.1 mm.
And hold it in preparation. The sample thus prepared is placed under the observation of a polarizing microscope with crossed Nicols. First, the temperature of the sample is lowered to room temperature (20 ° C.) or lower to bring the polymer composite solution on the slide glass into a state exhibiting optical anisotropy.
融点測定装置(YANAGIMOTO(株))を用い、
偏光顕微鏡で観察しながらサンプルの温度を徐々に(5
℃/min.)上昇させると、特定の温度において視野が暗
くなり光学的等方性の状態に変化したことが観察され
る。この時の温度を転移温度と名づける。Using a melting point measuring device (YANAGIMOTO CORPORATION),
Gradually increase the sample temperature (5
It is observed that the visual field became dark and changed to an optically isotropic state at a specific temperature when the temperature was increased by ° C / min.). The temperature at this time is named the transition temperature.
見掛け状光学的等方性の状態とは、偏光顕微鏡下で所定
の高分子溶液を観察していると最初、各種色あいの模様
を呈していたものが均一の色に変わり、しだいにその光
の強度は減少して暗くなるが、この時の均一の色からし
だいにその光の強度が減少して一定の暗さになるまでの
間の状態を示す。Apparent optical isotropic state means that when observing a predetermined polymer solution under a polarizing microscope, what initially had various shades of color changed to a uniform color, and the light gradually changed. Although the intensity decreases and becomes darker, it shows a state from the uniform color at this time until the intensity of the light gradually decreases to a constant darkness.
この状態を肉眼観察すると、外観的には透明で光学的等
方性のように見える。従ってこの状態を見掛け状光学的
等方性の状態と呼ぶことにする。When this state is observed with the naked eye, it appears to be transparent and optically isotropic in appearance. Therefore, this state is called an apparent optical isotropic state.
転移温度よりも高温の温度領域は光学的等方性を示す温
度領域であり、転移温度に達していない温度領域は、光
学的異方性を示す温度領域である。The temperature range higher than the transition temperature is a temperature range showing optical isotropy, and the temperature range not reaching the transition temperature is a temperature range showing optical anisotropy.
補強用高分子(A)の溶液中で占める濃度が低い場合に
は、該高分子複合体溶液は温度20℃以下にしても光学的
異方性への転移は生ぜず、光学的等方性を保持したまま
の状態を継続する。このような光学的異方性への転移を
生じない系では、良好な成形物を得ることができない。
逆に補強用高分子(A)の溶液中で占める濃度が高い場
合には、該高分子複合体溶液は温度210℃でも光学的等
方性への転移は生ぜず、光学的異方性を保持したままの
状態を継続する。When the concentration of the reinforcing polymer (A) in the solution is low, the polymer composite solution does not undergo a transition to optical anisotropy even at a temperature of 20 ° C. or less, and the optical isotropic property is obtained. Continue to hold. In a system in which such a transition to optical anisotropy does not occur, a good molded product cannot be obtained.
On the other hand, when the concentration of the reinforcing polymer (A) in the solution is high, the polymer composite solution does not undergo optical isotropic transition even at a temperature of 210 ° C. and has optical anisotropy. Continue to hold.
このような系では、たとえ210℃を越える温度にするこ
とで等方性溶液になったとしても補強用高分子(A)と
マトリックス高分子(B)が酸性溶媒中での分解が著し
くなり、良好な成形物は得られない。In such a system, the reinforcing polymer (A) and the matrix polymer (B) are remarkably decomposed in an acidic solvent, even if the solution becomes an isotropic solution when the temperature exceeds 210 ° C. Good molded products cannot be obtained.
本発明方法においては、補強用高分子(A),マトリッ
クス高分子(B)の種類、分子量の目安となる固有粘度
[η]あるいは特性粘度ηinh、溶媒及び各高分子の成
分比,濃度が決定されると、上記測定方法に従ってその
系の光学的異方性から光学的等方性への転移温度を測定
し、流延時の溶液温度を実質的に転移温度以下とし、流
延後該高分子溶液を転移温度以上に加熱し、見掛け状の
等方性溶液に転移後、凝固浴に浸漬するものである。光
学的異方性溶液を流延した状態では、補強用高分子がミ
クロに相分離した状態にある。In the method of the present invention, the types of the reinforcing polymer (A) and the matrix polymer (B), the intrinsic viscosity [η] or the characteristic viscosity ηinh, which is a standard of the molecular weight, the solvent and the component ratio and concentration of each polymer are determined. Then, the transition temperature from the optical anisotropy to the optical isotropy of the system is measured according to the above-mentioned measuring method, and the solution temperature at the time of casting is kept substantially below the transition temperature, and the polymer after casting The solution is heated above the transition temperature, transferred to an apparent isotropic solution, and then immersed in a coagulation bath. When the optically anisotropic solution is cast, the reinforcing polymer is microscopically phase-separated.
これを加熱し、等方性状態にもっていくことにより補強
用高分子及びマトリックス高分子が相互の相の中に溶け
込み、補強用高分子が極めて微小な集合体を形成するた
めの条件が整うことと推測される。By heating this and bringing it into an isotropic state, the reinforcing polymer and the matrix polymer will dissolve into each other's phase, and the conditions for the reinforcing polymer to form extremely minute aggregates will be set. Presumed to be.
これに反し、転移温度以上に加熱して光学的等方性とな
った高分子溶液を加熱された基板上に流延し、その後凝
固したものの成形物は延伸性が劣り、良好な力学特性を
示さない。凝固直前には、本発明の方法及び上記の等方
性溶液での流延法は、結果として同じように見えるが、
そのもたらすフイルムの力学特性においては顕著な差を
示す。この理由は定かではないが、本発明における如く
異方性溶液において流延し、その後加熱して等方性溶液
にもっていったものは、補強用ポリマーのマトリックス
ポリマーへのミクロ分散がより性能発現しやすい形で分
散しているためと思われる。Contrary to this, a polymer solution which is heated to a temperature not lower than the transition temperature to become optically isotropic is cast on a heated substrate, and then the solidified product has poor stretchability and good mechanical properties. Not shown. Immediately prior to coagulation, the method of the present invention and the casting method in the isotropic solution described above appear to be similar, but
The resulting mechanical properties of the film show a significant difference. The reason for this is not clear, but in the case of casting in an anisotropic solution as in the present invention and then heating to an isotropic solution, microdispersion of the reinforcing polymer into the matrix polymer is more effective. It seems that it is dispersed in a form that is easy to do.
成形方法としては、例えばガラス板または金属板等の固
い基盤上に流延する、あるいは布等のやわらかな基盤上
に流延してもよい。As a molding method, casting may be performed on a hard substrate such as a glass plate or a metal plate, or may be cast on a soft substrate such as a cloth.
連続的成膜方法としては、Tダイ等から押し出された高
分子溶液をベルト等の基板上に光学的異方性の状態で流
延し、その後熱風,ヒータ等で加熱して見掛け上の光学
的等方性の状態にもってゆきそれを凝固液中に浸漬する
ことによって製膜化することができる。As a continuous film forming method, a polymer solution extruded from a T-die or the like is cast onto a substrate such as a belt in an optically anisotropic state, and then heated with hot air or a heater to produce an apparent optical The film can be formed by bringing it into a state of isotropicity and immersing it in a coagulating liquid.
該高分子溶液を凝固するための凝固液としては、用いる
溶媒に非溶解性の溶媒を混合した系、例えば、硫酸水溶
液,メタンスルホン酸水溶液,リン酸水溶液等が挙げら
れる。As a coagulation liquid for coagulating the polymer solution, a system in which a solvent used is mixed with an insoluble solvent, for example, an aqueous solution of sulfuric acid, an aqueous solution of methanesulfonic acid, an aqueous solution of phosphoric acid and the like can be mentioned.
凝固上りの未延伸フイルムは、残存溶媒を十分に除いた
後、特に酸溶媒系ではアンモニアあるいは水酸化ナトリ
ウム等で中和処理することが必要である。The unstretched film that has just solidified needs to be neutralized with ammonia, sodium hydroxide or the like, especially in an acid solvent system, after the residual solvent is sufficiently removed.
乾燥フイルムは、その後フイルム等の延伸で用いられて
いる通常の延伸操作によって高モジュラスなフイルムと
なる。The dry film becomes a high-modulus film by a normal stretching operation that is then used for stretching the film or the like.
本発明において用いられる補強用高分子(A)とマトリ
ックス高分子(B)の割合はA/A+Bが5〜45%の範
囲にあるのがよい。補強用高分子(A)が5%よりも小
さい場合には、補強効果が小さく45%を越すと、補強用
高分子(A)の配向性が低下し本発明の特徴を発現する
ことができない。The ratio of the reinforcing polymer (A) and the matrix polymer (B) used in the present invention is preferably such that A / A + B is in the range of 5 to 45%. When the reinforcing polymer (A) is less than 5%, the reinforcing effect is small, and when it exceeds 45%, the orientation of the reinforcing polymer (A) is lowered and the characteristics of the present invention cannot be exhibited. .
本発明において用いられる固有粘度とは、100%硫酸も
しくはメタンスルホン酸もしくはクロルスルホン酸に補
強用高分子(A)の濃度が0.2g/100ccになるように溶解
後、30℃で常法により求めたηinhである。補強用高分
子(A)が上記の溶媒のいずれにも溶解する時は、その
中でもっとも低い値をその補強用高分子(A)の固有粘
度とする。The intrinsic viscosity used in the present invention is determined by a conventional method at 30 ° C. after dissolving in 100% sulfuric acid, methanesulfonic acid or chlorosulfonic acid so that the concentration of the reinforcing polymer (A) is 0.2 g / 100 cc. It is ηinh. When the reinforcing polymer (A) dissolves in any of the above solvents, the lowest value among them is the intrinsic viscosity of the reinforcing polymer (A).
以下に本発明の効果を実施例をもって示すが、実施例中
の百分率は、ことわらない限り重量基準である。繊維・
フイルムの機械的性質は、サンプル長4cmを毎分10%の
伸長速度で測定したものである。The effects of the present invention will be shown below with reference to examples, and the percentages in the examples are based on weight unless otherwise specified. fiber·
The mechanical properties of the film are measured with a sample length of 4 cm at an elongation rate of 10% per minute.
実施例1 補強用高分子(A)として、ポリ−p−フェニレンベン
ゾビスチアゾール(PPBTと略す)を常法に従って重
合し、メタンスルホン酸溶媒における固有粘度が4.1の
ものを得た。Example 1 As a reinforcing polymer (A), poly-p-phenylenebenzobisthiazole (abbreviated as PPBT) was polymerized by a conventional method to obtain a polymer having an intrinsic viscosity of 4.1 in a methanesulfonic acid solvent.
マトリックス高分子(B)は、3,4′−ジアミノジフェ
ニルエーテル(50モル%)とパラフェニレンジアミン
(50モル%)とをN−メチルピロリドンに濃度が6%に
なるようにして、乾燥窒素雰囲気下に溶解せしめ、5℃
に冷却した後、激しく撹拌しながらテレフタル酸ジクロ
ライドの粉末(100モル%)の当該溶液にすみやかに添
加し、35℃で1時間重合反応を行ない、これを水にて沈
澱し中和して得た。以下該ポリマーをPPOT−50と略
す。PPOT−50のηinhは硫酸溶媒で3.6であった。P
PBTとPPOT−50の成分比が30/70になるようにし
てメタンスルホン酸に溶解し、ポリマー全濃度が、6%
のものを作成した。該高分子複合体溶液の異方性から等
方性に転移する温度(相転移温度)は65℃であった。The matrix polymer (B) was prepared by adding 3,4'-diaminodiphenyl ether (50 mol%) and paraphenylenediamine (50 mol%) to N-methylpyrrolidone in a concentration of 6% under a dry nitrogen atmosphere. Dissolve in 5 ℃
After cooling to 50 ° C., the solution of terephthalic acid dichloride powder (100 mol%) was immediately added to the solution with vigorous stirring, and a polymerization reaction was carried out at 35 ° C. for 1 hour. It was Hereinafter, the polymer is abbreviated as PPOT-50. Ηinh of PPOT-50 was 3.6 in a sulfuric acid solvent. P
Dissolved in methanesulfonic acid so that the ratio of PBT and PPOT-50 was 30/70, and the total polymer concentration was 6%.
Created one. The temperature (phase transition temperature) at which the polymer complex solution undergoes isotropic transition from anisotropy was 65 ° C.
該高分子溶液をガラス基盤上にドクターナイフ(スリッ
ト幅100μm)を用いて室温で流延した。それを加熱板
に載せて、温度80℃まで昇温した。該高分子溶液がクロ
スニコルスの観察で均一の明るさからしだいに光の強度
が減少していく途中で凝固液に浸漬した。The polymer solution was cast on a glass substrate at room temperature using a doctor knife (slit width 100 μm). It was placed on a heating plate and the temperature was raised to 80 ° C. The polymer solution was immersed in the coagulation liquid while the intensity of light gradually decreased from the uniform brightness in the observation of crossed Nichols.
凝固液にはメタンスルホン酸の80%水溶液を用いた。凝
固上りフイルムは、水で十分に洗浄し水酸化ナトリウム
水溶液で中和後さらに24時間水で洗浄した。フイルムは
固定枠にはめて自然乾燥後、温度350℃,470℃でそれぞ
れ最大延伸倍率に0.8を乗じた延伸比で引張り一軸配向
フイルムを得た。An 80% aqueous solution of methanesulfonic acid was used as the coagulating liquid. The coagulated film was thoroughly washed with water, neutralized with an aqueous sodium hydroxide solution, and then washed with water for another 24 hours. The film was placed in a fixed frame, naturally dried, and then stretched at a temperature of 350 ° C. and 470 ° C. to obtain a stretched uniaxially oriented film at a draw ratio obtained by multiplying the maximum draw ratio by 0.8.
フイルムの力学特性は、フイルム厚み(μm)/モジュ
ラス(GPa)/伸度(%)/強度(GPa)=65/113
/1.2/1.0であった。The mechanical properties of the film are: film thickness (μm) / modulus (GPa) / elongation (%) / strength (GPa) = 65/113
It was /1.2/1.0.
実施例2〜4 実施例1において、ドクターナイフのスリット幅を2000
μm,4000μm,5000μmに変えた以外は同様の条件で
製膜し、一軸配向フイルムを得た。Examples 2 to 4 In Example 1, the slit width of the doctor knife was 2000.
Films were formed under the same conditions except that the thickness was changed to μm, 4000 μm, and 5000 μm to obtain a uniaxially oriented film.
フイルムの力学特性は表1に示す通りで良好なものが得
られた。The mechanical properties of the film were as shown in Table 1 and good ones were obtained.
比較例1,2 実施例1と同じようにして作られたPPBT/PPOT
−50の高分子溶液を温度80℃に保温されたガラス容器に
入れ、約20分間混合加熱し、該高分子溶液が光学的等方
性になっていることを確認後、80℃に保温された基板上
にドクターナイフ1000μm,2000μmで流延した。それ
を凝固浴中に入れ、その後の乾燥は実施例1と同一とし
た。 Comparative Examples 1 and 2 PPBT / PPOT prepared in the same manner as in Example 1
Put the polymer solution of -50 in a glass container kept at a temperature of 80 ° C, mix and heat for about 20 minutes, and after confirming that the polymer solution is optically isotropic, keep it at 80 ° C. It was cast on a substrate with a doctor knife of 1000 μm and 2000 μm. It was placed in a coagulation bath and the subsequent drying was the same as in Example 1.
一軸配向物のフイルムの力学特性は、ドクターナイフ10
00μmからのものが膜厚(μm)/モジュラス(GP
a)/伸度(%)/強度(GPa)=65/85/2.1/1.2で
あった。The mechanical properties of the uniaxially oriented film are as follows: Doctor Knife 10
Film thickness (μm) / modulus (GP) from 00μm
a) / elongation (%) / strength (GPa) = 65/85 / 2.1 / 1.2.
ドクターナイフ2000μmから流延したものは、凝固上り
フイルム中にマルタ十字が多数認められ延伸が不良であ
った。The film cast from a doctor knife of 2000 μm had a large number of Maltese crosses in the solidified film and was poorly stretched.
Claims (1)
らなる補強用高分子(A)と融着性を有するマトリック
ス高分子(B)とを主として含有する高分子溶液を、基
板上に流延し、次いで凝固浴中に導入し、製膜すること
からなる高分子複合体の製造法において、当該高分子溶
液が光学的等方性を示す温度領域と光学的異方性を示す
温度領域とを有するものであり、基板上に流延する際の
当該高分子溶液の温度は光学的異方性を示す温度領域内
にあり、流延後、当該高分子溶液を加熱することで見掛
け状光学的等方性に転移せしめつつ凝固浴中に導入して
製膜することを特徴とする高分子複合体の製造法。1. A polymer solution mainly containing a reinforcing polymer (A) substantially composed of a polyazole having a rod-like skeleton and a matrix polymer (B) having a fusion property is cast on a substrate. Then, in a method for producing a polymer composite, which comprises introducing into a coagulation bath to form a film, a temperature range in which the polymer solution exhibits optical isotropy and a temperature range in which optical anisotropy is exhibited. The temperature of the polymer solution at the time of casting on the substrate is within a temperature range showing optical anisotropy, and after casting, the polymer solution is heated to give an apparent optical effect. A method for producing a polymer composite, which comprises introducing a film into a coagulation bath while transferring it isotropically to form a film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14329087A JPH0637562B2 (en) | 1987-06-10 | 1987-06-10 | Polymer composite manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14329087A JPH0637562B2 (en) | 1987-06-10 | 1987-06-10 | Polymer composite manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63308040A JPS63308040A (en) | 1988-12-15 |
| JPH0637562B2 true JPH0637562B2 (en) | 1994-05-18 |
Family
ID=15335289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14329087A Expired - Lifetime JPH0637562B2 (en) | 1987-06-10 | 1987-06-10 | Polymer composite manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0637562B2 (en) |
-
1987
- 1987-06-10 JP JP14329087A patent/JPH0637562B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63308040A (en) | 1988-12-15 |
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