JPH0689159B2 - Polymer composite manufacturing method - Google Patents
Polymer composite manufacturing methodInfo
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- JPH0689159B2 JPH0689159B2 JP10017789A JP10017789A JPH0689159B2 JP H0689159 B2 JPH0689159 B2 JP H0689159B2 JP 10017789 A JP10017789 A JP 10017789A JP 10017789 A JP10017789 A JP 10017789A JP H0689159 B2 JPH0689159 B2 JP H0689159B2
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- polymer
- film
- water
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- reinforcing
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Description
【発明の詳細な説明】 〈産業上の利用分野〉 本発明は耐荷重構造用材料等として有用な高分子複合体
の製造法に関する。DETAILED DESCRIPTION OF THE INVENTION <Industrial Field of Application> The present invention relates to a method for producing a polymer composite useful as a load bearing structural material or the like.
〈従来の技術〉 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。<Prior Art> 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、そこの存在する欠陥は
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 and lead to the destruction of the composite material.
かかる欠陥を解決するために、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
高分子複合耐を製造することが検討されてきた。In order to solve such a deficiency, instead of a 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 resistant product in which the reinforcing polymer is dispersed and mixed in an extremely microscopic state and the reinforcing polymer is oriented by molding.
本発明者らは、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の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 used, as an organic polymer fiber, a polymer for reinforcing a polyazole-based polymer such as poly-p-phenylene benzobisthiazole, which gives an excellent tensile modulus, in a combination system with various matrix polymers. Although studies have been conducted on increasing the modulus, there were drawbacks such as a lower tensile modulus than the expected additivity value when both polymer components were sufficiently oriented. Also,
In order to obtain a molded article 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, when the thickness is increased, the coagulability deteriorates, No good film was obtained.
〈発明が解決しようとする課題〉 本発明の目的は、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ロアゾール系高
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
膜化を達成することにある。<Problems to be Solved by the Invention> An object of the present invention is to solve the above problems.
It is to achieve high modulus and thick film in a system using a polylene-based polymer such as phenylenebenzobisthiazole as a reinforcing polymer and a flexible polymer as a matrix polymer.
〈課題を解決するための手段〉 本発明者は、高性能の機械的、熱的物性を有する高分子
複合体を得るべく鋭意研究の結果、強固前の高分子溶液
に凝固浴組成の一成分である水をあらかじめ適切な量を
含有させて製膜すると、厚膜でも優れた高分子複合体が
得られることを見出し本発明に達成した。<Means for Solving the Problems> The inventors of the present invention have earnestly studied to obtain a polymer composite having high-performance mechanical and thermal properties, and as a result, one component of the coagulation bath composition was added to the polymer solution before solidification. It was found that when an appropriate amount of water is contained in advance to form a film, an excellent polymer composite can be obtained even in a thick film.
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)、融着性を有するマトリッ
クス高分子(B)及び溶媒(C)を主として含有する高
分子溶液を、水を含む凝固浴中に導入し、製膜すること
からなる高分子複合体の製造法において、溶媒(C)中
にあらかじめ水を少くとも1(重量)%以上含有せしめ
ることを特徴とする高分子複合体の製造法に関する。That is, according to the present invention, a polymer solution mainly containing a reinforcing polymer (A) substantially composed of a polyazole having a rod-like skeleton, a matrix polymer (B) having a fusion property and a solvent (C) is treated with water. In a method for producing a polymer composite, which comprises introducing into a coagulation bath containing water and forming a film, the polymer composite is characterized in that the solvent (C) contains water at least 1 (wt)% or more in advance. Regarding the manufacturing method of the body.
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−NH−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あげられ
る。The reinforcing polymer (A) used in the present invention has the following formula [Wherein, X represents -S-, -O- or -NH-,
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 the specification of No. 7,407, and polyazoles such as poly-p-phenylene benzobisthiazole, poly-p-phenylene benzoxazole, and poly-p-phenylene benzobisimidazole can be mentioned.
補強用高分子(A)の分子量は通常分子量の目安なる固
有粘度が1以上であり、好ましくは2以上である。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 2 or more.
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類、ポリヘキサメチ
レンイソフタルアミド等の芳香族ポリアミド類、エーテ
ル基等の屈曲性基を導入した屈曲性芳香族ポリアミド
類、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 soluble in the same solvent as the reinforcing polymer (A). Nylon 6, nylon 66, nylon 610, nylon 1
2.Nylon 11 and other aliphatic polyamides, polyhexamethylene isophthalamide and other aromatic polyamides, ether groups and other flexible group-introducing flexible aromatic polyamides, polyester, polycarbonate, polyvinyl acetate, polysulfone, poly Examples thereof include ether sulfone, polyether imide, polyether ketone, polyphenylene sulfide, and the like.
溶媒(C)としては、補強用高分子(A)とマトリック
ス高分子(B)との共通溶媒が用いられる。かかる共通
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。A common solvent for the reinforcing polymer (A) and the matrix polymer (B) is used as the solvent (C). The common solvent may be any solvent that can dissolve the constituent polymers, and examples thereof include concentrated sulfuric acid and an acidic solvent of methanesulfonic acid. These may be appropriately mixed and used.
これらの溶媒(C)中に、凝固浴成分である水を1(重
量)%以上含有しなければならない。また、あまりに水
を多く含有することも好ましくなく、通常は8%以下で
ある。Water (coagulation bath component) must be contained in an amount of 1 (wt)% or more in these solvents (C). Further, it is not preferable to contain too much water, and it is usually 8% or less.
凝固浴としては、水単独及び上記溶媒(C)と水との混
合水溶液が好ましい。The coagulation bath is preferably water alone or a mixed aqueous solution of the solvent (C) and water.
本発明方法では凝固する前の高分子溶液中にあらかじめ
水を特定量含有させる。これによって厚膜にしても均一
な凝固上りの膜形成が可能となり、高モジュラスのフイ
ルムが得られる。In the method of the present invention, a specific amount of water is previously contained in the polymer solution before solidification. As a result, even if the film is thick, it is possible to form a film with a uniform solidification and a high modulus film can be obtained.
さらに、本発明方法においては、相転移過渡製膜法と組
合せることによりさらにその効果を発揮することが可能
となる。Furthermore, in the method of the present invention, the effect can be further exhibited by combining with the phase transition transient film formation method.
即ち、当初室温状態において光学的異方性を有する高分
子溶液を加熱していくと、適切なポリマー濃度範囲にあ
るものは50〜90℃の温度範囲において光学的等方性に転
移する。この状態の溶液から該高分子溶液がその温度雰
囲気におかれるならば、光学的異方性となる温度を有す
る凝固浴中に浸漬すると、該高分子溶液は等方性から異
方性相への過渡状態で凝固し、力学特性の優れた成形物
を得ることが可能となる。That is, when a polymer solution having optical anisotropy is heated initially at room temperature, a polymer having an appropriate polymer concentration range is optically isotropic in a temperature range of 50 to 90 ° C. If the polymer solution is exposed to the temperature atmosphere from the solution in this state, the polymer solution is transformed from an isotropic phase to an anisotropic phase when immersed in a coagulation bath having a temperature at which optical anisotropy occurs. It is possible to obtain a molded product having excellent mechanical properties by solidifying in the transient state of.
本発明方法において、高分子溶液中に水を含有させると
その相転移の温度が低下し、低下した分だけさらにポリ
マー濃度を高めることができ、これは良好な成形物を得
る上で好ましい。In the method of the present invention, when water is contained in the polymer solution, the temperature of its phase transition is lowered, and the polymer concentration can be further increased by the lowered amount, which is preferable for obtaining a good molded product.
高分子溶液中に水を含有させるもう一つの効果は、その
高分子溶液の溶液粘度が著しく低減することである。溶
液粘度が低減することで、製膜時の溶液の流動性が安定
し、さらにはポリマー濃度の増加が可能となる。これら
二つの効果により凝固浴の成分を含有してなる高分子溶
液から製膜したものは優れた性能の成形物を得ることが
可能となる。Another effect of including water in the polymer solution is to significantly reduce the solution viscosity of the polymer solution. By reducing the solution viscosity, the fluidity of the solution during film formation is stabilized, and the polymer concentration can be increased. Due to these two effects, a film formed from a polymer solution containing the components of the coagulation bath can obtain a molded product with excellent performance.
製膜方法としては、Tダイ等から押出された高分子溶液
を凝固浴中に直接浸漬してもよいし、或いはドラム上に
流延後、そのドラムを凝固浴中に浸漬させてもよい。凝
固上りの未延伸フイルムは、残存溶液を十分に除いた
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。As a film forming method, the polymer solution extruded from a T-die or the like may be directly immersed in the coagulation bath, or after casting on a drum, the drum may be immersed in the coagulation bath. The unstretched film after solidification needs to be neutralized with ammonia, sodium hydroxide or the like, especially in an acid solvent system, after sufficiently removing the residual solution.
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.
本発明においても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(重
量)%の範囲にあるのがよい。補強用高分子(A)が5
(重量)%より小さい場合には、補強効果が小さく45
(重量)%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困難となる。The ratio of the reinforcing polymer (A) and the matrix polymer (B) used in the present invention is preferably in the range of 5 to 45 (wt)% A / A + B. Reinforcing polymer (A) is 5
If it is less than (weight)%, the reinforcing effect is small.
When it exceeds (weight)%, the orientation of the reinforcing polymer (A) is lowered and it becomes difficult to exhibit the characteristics of the present invention.
〈発明の効果〉 以上の如き本発明方法によれば、あらかじめ高分子溶液
中に水を1(重量)%以上含有させることにより、該高
分子溶液の相転移温度が低下し、溶液粘度も低減するた
め、膜厚で力学特性の優れたフイルム成形物を製造する
ことができる。<Effects of the Invention> According to the method of the present invention as described above, by preliminarily containing 1 (wt)% or more of water in the polymer solution, the phase transition temperature of the polymer solution is lowered and the solution viscosity is also reduced. Therefore, it is possible to manufacture a film molded product having excellent film thickness and mechanical properties.
〈実施例〉 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。<Examples> The effects of the present invention will be shown below with 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.
また、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、その中で最も低い値をそ
の補強用高分子(A)の固有粘度とする。Also, the intrinsic viscosity is ηinh obtained by a usual method at 30 ° C. after dissolving in 100% sulfuric acid or methanesulfonic acid or chlorosulfonic acid so that the concentration of the reinforcing polymer (A) is 0.2 g / 100 cc. is there. 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).
〈実施例1〜3、比較例1〉 補強高分子(A)として、ポリ−p−フェニレンベンゾ
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。<Examples 1 to 3 and Comparative Example 1> As the reinforcing polymer (A), poly-p-phenylenebenzothiazole (abbreviated as PPBT) was polymerized according to a conventional method, and an intrinsic viscosity in a methanesulfonic acid solvent was 4.1. Obtained.
マトリックス高分子(B)は、3,4′−ジアミノフェニ
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、激しく攪拌しながらテレフタル酸ジクロライ
ドの粉末(100モル%)を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。PPO
T-50のηinhは硫酸溶媒で3.6であった。The matrix polymer (B) consists of 3,4'-diaminophenyl ether (50 mol%) and paraphenylenediamine (50
Mol%) and N-methylpyrrolidone in a concentration of 6% and dissolved in a dry nitrogen atmosphere, and after cooling to 5 ° C., terephthalic acid dichloride powder (100 mol%) was stirred vigorously. The solution was promptly added to the solution, a polymerization reaction was carried out at 35 ° C. for 1 hour, and the solution was precipitated with water and neutralized. Hereinafter, the polymer is abbreviated as PPOT-50. PPO
Ηinh of T-50 was 3.6 in sulfuric acid solvent.
PPBT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た。なお、メタンスルホン酸の初期
水分率は0.4%でありこれに水を添加してメタンスルホ
ン酸中の水分率が1.5、2.5、3.5、4.5%のものを作成
し、ポリマー全濃度は6.6%になるよう高分子溶液を調
製した。水分率0.4%のものの異方性から等方性相へ転
移する温度(相転移温度)は98℃であったが、水を1.5
%、2.5%、3.5%、4.5%と添加するにつれて、相転移
温度は83℃、78℃、72℃、65℃と低下した。また溶液粘
度も水分率0.4%では11万ポイズであったが水分率1.5〜
4.5%では7500〜5000ポイズと著しく粘度低下すること
が認められた。PPBT and PPOT-50 were dissolved in methanesulfonic acid so that the component ratio was 30/70. The initial moisture content of methane sulfonic acid was 0.4%, and water was added to this to create methane sulfonic acid with a moisture content of 1.5, 2.5, 3.5, 4.5%, and the total polymer concentration was 6.6%. A polymer solution was prepared so that The temperature at which a water content of 0.4% changes from anisotropy to an isotropic phase (phase transition temperature) is 98 ° C, but water is 1.5%.
%, 2.5%, 3.5%, 4.5%, the phase transition temperatures decreased to 83 ℃, 78 ℃, 72 ℃ and 65 ℃. The solution viscosity was 110,000 poise when the water content was 0.4%, but the water content was 1.5-
At 4.5%, it was confirmed that the viscosity was remarkably reduced to 7500 to 5000 poise.
該高分子溶液をプランジャーに押し込み、各水分率の含
有量に応じて表1に示す温度にTダイを加熱し、空気層
を介して凝固浴中に押し出した。凝固浴はメタンスルホ
ン酸60%水溶液の45℃を第1段の浴として、第2段浴と
してメタンスルホン酸30%水溶液の30℃とした。The polymer solution was pushed into a plunger, the T-die was heated to the temperature shown in Table 1 according to the content of each moisture content, and extruded into a coagulating bath through an air layer. As the coagulation bath, 45 ° C. of a 60% aqueous solution of methanesulfonic acid was used as the first stage bath, and 30 ° C. of a 30% aqueous solution of methanesulfonic acid was used as the second stage bath.
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400℃で最大延伸倍
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。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, air-dried, and then stretched at a temperature of 400 ° C. to obtain a stretched uniaxially oriented film at a stretching ratio of 0.8.
表1に各フイルムの物性を示すが、これらの結果から凝
固浴成分の水をあらかじめ溶液中に1.0%以上含有させ
ることによりテープ性能が向上することが認められる。Table 1 shows the physical properties of each film. From these results, it is recognized that the tape performance is improved by preliminarily containing 1.0% or more of the coagulation bath component water in the solution.
Claims (2)
らなる補強高分子(A)、融着性を有するマトリックス
ポリマー(B)及び溶媒(C)を主として含有する高分
子溶液を、水を含む凝固浴中に導入し、製膜することか
らなる高分子複合体の製造法において、溶媒(C)中に
あらかじめ水を少くとも1(重量)%以上含有せしめる
ことを特徴とする高分子複合体の製造法。1. A polymer solution containing mainly a reinforcing polymer (A) substantially composed of a polyazole having a rod-like skeleton, a fusible matrix polymer (B) and a solvent (C), and coagulating the polymer solution with water. In a method for producing a polymer composite, which comprises introducing into a bath to form a film, the solvent (C) contains water in advance at least 1 (wt)% or more. Manufacturing method.
量)%含有せしめることを特徴とする請求項1記載の高
分子複合体の製造法。2. The method for producing a polymer composite according to claim 1, wherein water (1) is contained in the solvent (C) in advance in an amount of 1 to 8% by weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10017789A JPH0689159B2 (en) | 1989-04-21 | 1989-04-21 | Polymer composite manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10017789A JPH0689159B2 (en) | 1989-04-21 | 1989-04-21 | Polymer composite manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02281077A JPH02281077A (en) | 1990-11-16 |
| JPH0689159B2 true JPH0689159B2 (en) | 1994-11-09 |
Family
ID=14267032
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10017789A Expired - Fee Related JPH0689159B2 (en) | 1989-04-21 | 1989-04-21 | Polymer composite manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0689159B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69231159D1 (en) * | 1991-04-01 | 2000-07-13 | Foster Miller Inc | EXTRUDED THERMOPLASTICS, LIQUID CRYSTALLINE POLYMERS AND COMPOSITIONS THEREOF WITH PLANNIC MORPHOLOGY |
-
1989
- 1989-04-21 JP JP10017789A patent/JPH0689159B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02281077A (en) | 1990-11-16 |
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