JPS59120620A - Production of new polymer composition - Google Patents

Production of new polymer composition

Info

Publication number
JPS59120620A
JPS59120620A JP22665282A JP22665282A JPS59120620A JP S59120620 A JPS59120620 A JP S59120620A JP 22665282 A JP22665282 A JP 22665282A JP 22665282 A JP22665282 A JP 22665282A JP S59120620 A JPS59120620 A JP S59120620A
Authority
JP
Japan
Prior art keywords
polymer
carbon fiber
monomer
electrolyte
epoxy compound
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
JP22665282A
Other languages
Japanese (ja)
Other versions
JPH0145490B2 (en
Inventor
Kazuo Kishida
岸田 一夫
Isao Sasaki
笹木 勲
Hajime Asai
浅井 肇
Nobuhiro Mukai
向 信博
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.)
Mitsubishi Rayon Co Ltd
Original Assignee
Mitsubishi Rayon Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Rayon Co Ltd filed Critical Mitsubishi Rayon Co Ltd
Priority to JP22665282A priority Critical patent/JPS59120620A/en
Priority to EP83110347A priority patent/EP0106352B1/en
Priority to DE8383110347T priority patent/DE3380065D1/en
Priority to US06/542,950 priority patent/US4510024A/en
Publication of JPS59120620A publication Critical patent/JPS59120620A/en
Publication of JPH0145490B2 publication Critical patent/JPH0145490B2/ja
Granted legal-status Critical Current

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  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
  • Reinforced Plastic Materials (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Polymerisation Methods In General (AREA)
  • Graft Or Block Polymers (AREA)
  • Epoxy Resins (AREA)

Abstract

PURPOSE:To obtain a polymer consisting of carbon fiber and an epoxy polymer which are strongly united, by using a cycloaliphatic epoxy compound as at least part of a reactive monomer and electrolytically polymerizing the monomer by using carbon fiber as an electrode. CONSTITUTION:A cycloaliphatic epoxy compound of, for example, formula I or II(wherein R1 is a group of formula III, R3 is a 1-20C alkylene, R2 is a 1-30C alkyelen, and R4 is a 30C or lower alkylene) is used as at least part of a reactive monomer, and the monomer and a strongly electrolytic inorganic salt (e.g., sodium nitrate) are dissolved in a solvent. The resulting solution is poured into a electrolytic polymerization apparatus 5 as an electrolyte 4. Carbon fiber rovings 3 are immersed in the electrolyte 4 and a D.C. current is passed between the electrolyte 4 and the carbon fiber 3. Thus the reaction mixture is electrolytically polymerized to obtain the purpose polymer composition consisting of the carbon fiber 3 and the epoxy polymer which are strongly united.

Description

【発明の詳細な説明】 本発明は電解重合法により、炭素繊維似下CFと略す)
と有機重合体が、強固に合一・化された新規な重合体組
成物の製造法に関する。
[Detailed Description of the Invention] The present invention uses electrolytic polymerization to produce carbon fiber (abbreviated as CF).
This invention relates to a method for producing a novel polymer composition in which the organic polymer and the organic polymer are strongly combined and combined.

従来、鉄、銅及び銀等の金属を電極とI〜で、反応性モ
ノマーを電解重合することにより、金属−有機重合体を
製造する方法は公知であるが、モノマーの重合活性が低
く、゛まだ金属へのポリマー付着量が著しく少ないため
、工業的観点からし」1、はとんど実用に供し得ないも
のであった。
Conventionally, there has been a known method for producing metal-organic polymers by electrolytically polymerizing reactive monomers of metals such as iron, copper, and silver with electrodes and I~, but the polymerization activity of the monomers is low and Since the amount of polymer attached to the metal was still extremely small, from an industrial point of view, it could hardly be put to practical use.

本発明者等は、上述した現状に鑑み、鋭意検討1、た結
ψ、C2市、↑/1掻有−するC11″を7111極と
1〜で、環戊脂tlJ−i族]−ボギン化合物を反応性
モ、ツマ−の一部ま/こ11 □f部と1.−U用いる
ととにより、反応性モノマーの重合油t’t、 i−茗
る1〜〈高め、電極であるCp’にイ」伏型合体が多量
−に、かつ強固に合一化し、さら(7j−1イズ効甲の
優オtた従来方法では得られない新規な重合体組成物が
得られることを見出し7、本発明に二完成−するに至゛
)た。
In view of the above-mentioned current situation, the present inventors conducted intensive study 1, and determined that C11'' with ψ, C2 city, ↑/1 has 7111 poles and 1 ~, ring fat tlJ-i group]-bogin By using the compound as a reactive monomer, a part of the reactive monomer, a part of the 11 □f part and 1.-U, the polymerized oil of the reactive monomer is created. It has been shown that a large amount of I'-type polymers are strongly integrated with Cp', and that a new polymer composition which cannot be obtained by conventional methods and which has superior effects of 7j-1 is obtained. Heading 7: The present invention has now been completed.

従来、2f’J’i以上の素材の複合化により、構成力
+」の特14tを・相互に補い、新しい有効な機能舎牛
み出す複合材Hの開発が盛んに行なわれている中にあっ
て、有機重合体の強化、充填拐として有用なC11″と
の複合化に関しては、例ズば機械的強度、リリI何率、
熱変形温度、′電気的特性等広範にわたる’l’1fj
li改良が報告されている。しか17ながら、この場合
、複合化素材相互の諸性質を著るしく異にするため、相
溶性、接着性等の界面親和性に乏しく、充分な複合効果
全発揮する?−とができない現状にある。
Conventionally, by compositing materials of 2f'J'i or more, the development of composite materials H that mutually complement each other and bring out new effective functions has been actively carried out. Regarding compounding with C11'', which is useful as reinforcement and filler for organic polymers, for example, mechanical strength, Lili I percentage,
A wide range of thermal deformation temperatures, electrical properties, etc.
li improvements have been reported. However, in this case, since the properties of the composite materials are significantly different from each other, interfacial compatibility such as compatibility and adhesiveness is poor, and the full composite effect is not fully exerted. -The current situation is that it is impossible to do so.

この点を改良するために、無機酸類による酸化処即全施
(〜だ(31P表面・−・、のビニ二〕1グラノド法、
c[vに高エネルギー放射線を照射して41機重合体を
グラフト化さぜる放射線法等に4しり、イJ機高分子−
物質とCFとの界面親和性を向上さ什る試みがなされて
いるが、反応に長時間を・安し、斗だ放射線発生装置雪
を必要とするため、]−: (′T!の類4イF化及び
製造コストの大+iな増大とに、る等、実用性向で大き
な問題点を治し−Cいる。
In order to improve this point, oxidation treatment with inorganic acids was carried out immediately (~da (31P surface...) 1 Granod method,
c
Attempts have been made to improve the interfacial affinity between substances and CF; This solves major problems in terms of practicality, such as the shift to 4F and the large increase in manufacturing costs.

本発明は、上記問題点を解決しまたものであっ)で、環
式脂肪族エポキシ化合物を反応f4モノマーの−・部ま
たC1全部としで用いることを特徴とJ゛る(冊Cとエ
ポキシ重合体が強固に合一化された重合体組成物の製造
法を提供するものである。
The present invention solves the above-mentioned problems and is characterized by using a cycloaliphatic epoxy compound as part of the reaction f4 monomer or as the entire C1 (Book C and epoxy polymer). The present invention provides a method for producing a polymer composition that is strongly integrated.

一般に、支持電解質を加えた条f’tドでありでも、反
応性千ツマ−の電解重合を実施−する場合、長15間の
重合時間経過後においても、・その取合率C」、がなり
低い水準であるのに対し、本発明によれば、環式脂肪族
エボWン化合物を反応性モノマーの−・部−または全部
と(〜て、添加することにより、極めて特異な重合活性
をもたらし、数秒で実用的に価値のある高重合率の重合
体が、CF衣表面多量生成するとともに、サイズ効果が
優れているために集束1′1が極めて向上するものであ
る。
In general, even if a supporting electrolyte is added, when carrying out electrolytic polymerization of 1,000 reactive polymers, even after a polymerization time of 15 minutes has elapsed, the proportion C' In contrast, according to the present invention, by adding a cycloaliphatic ebon compound to part or all of the reactive monomer, a very specific polymerization activity can be achieved. In a few seconds, a polymer with a high polymerization rate, which is of practical value, is produced in large quantities on the surface of the CF coating, and because of its excellent size effect, the focusing 1'1 is greatly improved.

更に、本発明の特徴は、OFの表面と、本発明方法によ
って施される重合体との間の相互作用が中純な吸着など
の意味における接着を超えて、強固に合一化される点に
ある。
Furthermore, the present invention is characterized in that the interaction between the surface of the OF and the polymer applied by the method of the present invention goes beyond adhesion in the sense of pure adsorption, and is strongly integrated. It is in.

本発明の、実施態様の一例を挙げると、溶媒に反応性モ
ノマー及び支持電解質と(〜て強電解質無機塩を溶解し
て調整した電解浴中に、CFロー ピングを浸゛漬し、
該電解液とCF間に直流電圧を通電することにより、該
OF衣表面、反応性モノマーの電S重合反応を生ぜしめ
、所定の重合時間をもって高い取合率で、該ay衣表面
該反応性モノマーの重合体にて均一、多量に、(−かも
強固に固着化させることができる。この際、上記3成分
を共肴トに通電させることが必須条件となるが、必−1
’Lも同時に通電せしめる必要はない。即ち、例えば強
1(L解刊無機塩による前処理を施(〜たOFを使用し
一部も、本発明方法により、モノマーの重合時において
、新たな無機塩を添加することなく、同様の重合体組成
物を得ることができる。
To give an example of an embodiment of the present invention, a CF roping is immersed in an electrolytic bath prepared by dissolving a reactive monomer and a supporting electrolyte (-) and a strong electrolyte inorganic salt in a solvent,
By applying a DC voltage between the electrolyte and the CF, an electrolytic polymerization reaction of the reactive monomer on the surface of the OF coating is caused, and the reactive monomer on the surface of the OF coating is produced at a high polymerization rate within a predetermined polymerization time. Polymer monomers can be used to bond uniformly, in large quantities, and firmly (-).In this case, it is an essential condition that the above three components are energized together, but it is necessary to
It is not necessary to energize 'L at the same time. That is, for example, some of the OFs pretreated with inorganic salts can be used in the same way without adding new inorganic salts during monomer polymerization according to the method of the present invention. A polymer composition can be obtained.

従来、無機酸あるいは無機塩類を支持電解質として、同
様の重合体組成物を得る方法t、1公知であるが、千ツ
マ−の重合活性が低く、またa 1rへのポリマー付着
量が著るしく小さいため、サイズ効果が発現されないと
いった工業的実用性に関する欠点を有している。これら
の問題点に関し゛L1本発明方法は、特定のエポキシ化
合物を反応性モノマーの一部または全部として用いるこ
とにより、CF衣表面、生成有機重合体が、多聞に、か
つ強固に合一化し、さらに驚くべきことに、生成重合体
組成物のサイズ効果が、抜群であるために、c]t’繊
維間の収束性が、極めて良好な生成物を得る方法を提供
するものである。
Conventionally, there is a known method of obtaining a similar polymer composition using an inorganic acid or an inorganic salt as a supporting electrolyte, but the polymerization activity of the polymer is low, and the amount of polymer adhering to the a1r is significant. Since it is small, it has a disadvantage in terms of industrial practicality, such as not exhibiting a size effect. Regarding these problems, the method of the present invention uses a specific epoxy compound as part or all of the reactive monomer, so that the surface of the CF coating and the produced organic polymer are often and strongly integrated. More surprisingly, the size effect of the resulting polymer composition is so outstanding that it provides a method for obtaining a product with very good convergence between c]t' fibers.

本発明に用いられる特定のエポキシ化合物と[7ては、
生成ポリマーとCFとの強固なる合−性、及びマトリッ
クス樹脂との反応性等を発現させる活性サイドとI〜で
、多官能性を有(−かっ、環式化合物であることが好ま
しく、ビスーエボキシシク11ヘキシル力ルポギシレー
 ト類、ビスーエボキゾゾクロー\キー′ル・ジ・カル
ボ片シシ/−1・類、及ヒビスーエボギシシク11ヘギ
シルジオギサン類等が、顕著な゛リーイズ効唱を発現し
7、かつ電解重合活性も高く々了ま(7い。
The specific epoxy compound used in the present invention [7]
It has a polyfunctionality (-, preferably a cyclic compound, and a bis-epoxy Hexyl-11-hexyllupoglycylates, bis-evoxozochlores, key-le-di-carb-1-1, and hibis-evogysyl-11-hexyldiogysanes have a remarkable effect. 7, and the electrolytic polymerization activity was also very high (7).

本発明(・で用いられる炭素繊維とl−では、ポリアク
リロごl・ソノ1又シJ、その共1c合体からなる高強
度あるいに1:、高弾性CF、石油高温分解ピッチ、コ
ールタールピノ°fおよび石炭解重合物を原料とするO
F、更には気相成長法によるCFなどが挙げられ、炭素
質、黒鉛質OFいずJl、も適用可能である。寸だ各種
CFは通常実施される表面酸化処理を施こ17てあって
もよい。又、導電41ケ有−する鉄、銀、ステンレス、
銅アルミニウム等の金属繊維も適用できる。線維形態は
ロービング状長繊維形態が好寸しく、繊維径V1特に限
定されない。本発明によって得られる複合体は、いずJ
l、も界面接着性が良好で、かつ取扱い作業性の優れた
収束組成物として得られる。
The carbon fibers used in the present invention (・) include polyacrylic fibers, polyacrylic fibers, polyacrylic fibers, high-strength carbon fibers made of a combination of both, high-elastic CF, petroleum high-temperature decomposition pitch, coal tar pinot. °f and O made from coal depolymerized material
Examples include F, and further CF produced by a vapor phase growth method, and carbonaceous and graphite OF is also applicable. Various types of CF may be subjected to a commonly performed surface oxidation treatment17. In addition, there are 41 conductive metals such as iron, silver, stainless steel,
Metal fibers such as copper aluminum can also be applied. The fiber form is preferably a roving-like long fiber form, and the fiber diameter V1 is not particularly limited. The complex obtained by the present invention is
1 can also be obtained as a convergent composition with good interfacial adhesion and excellent handling workability.

本発明に用いられる共反応性千ツマ−は特に限定されな
いが、具体的には、通常のラジカル重合しつるヒニル申
量体及びアジリジン環含有化合物等が適用できる。
The co-reactive polymer used in the present invention is not particularly limited, but specifically, common radical polymerizable monomers, aziridine ring-containing compounds, etc. can be used.

本発明によれば、電解液中の環式脂肪族ユ、ボキシ化合
物の濃度は約()05〜100重量φ、好ま(〜くけ0
1〜50重駄チ、特に好ましくけ、05〜30重量%の
溺で使用される。使用−するcFに対−する反応性モノ
マー(環式脂肪族エポキシ化合物)も(−<は、反応性
土ツマー混合物の重駐比は、広範囲に変えることができ
、約500:1乃ヤ1: 5 (1(1、好i Lll
JJ5 o : 1−乃’!約1. : 5 。
According to the present invention, the concentration of the cycloaliphatic compound in the electrolyte is approximately ()05 to 100 wt.
It is used at a concentration of 1 to 50% by weight, particularly preferably 05 to 30% by weight. The reactive monomer (cycloaliphatic epoxy compound) to cF used can also be used. : 5 (1 (1, good i Lll
JJ5 o: 1-no'! Approximately 1. : 5.

である。溶媒の聞ij:OFとモノマー=との総重量に
基づき、約0.9”1%乃至数千倍、好t L < シ
ま約1係〜ioo倍である。電解重合は、反応性モノマ
ーを含む電解液とCF間に直流電流を通知、し7て行な
うが、その際の電流密度Vよ、通常001〜2゜A /
 dn? 、好ましくは0.1− = 2 A / d
yyz2であり、電圧は通常5〜25V程度である。電
流密度が、あ1り低いと重合速度が遅くなり好寸(−<
ない(7、逆に電流密度が、あ1り高くなりすぎると、
OF’自身が劣化するため好ましくない。又、CFは陽
イ愼及び陰極のいずれの電位でも適用できる。反応時間
は約01秒乃至約5時間である。反応温度は約−50U
〜T−(10C1好寸t、 < &、j、OC〜SOC
で行なわれる。ここで具体的な反応温度は、用いる反応
性王ツマ−によって適宜選択されるが、熱重合が無視で
きる程度に抑制される温度で実施することが重要であり
、極端に熱重合がおこる様な高温−C実施する場合、生
成複合体の合−性及び均一性はl511害される。生成
複合体は約10〜300C1好−よ[7くは約:(0〜
2007:の温度範囲で乾燥することができる。
It is. The amount of solvent is about 0.9"1% to several thousand times, preferably about 1 to iooo times, based on the total weight of OF and monomers. Electrolytic polymerization A direct current is applied between the electrolyte containing the CF and the CF, and the current density V at that time is usually 001~2°A
dn? , preferably 0.1- = 2 A/d
yyz2, and the voltage is usually about 5 to 25V. If the current density is too low, the polymerization rate will be slow, resulting in a good size (-<
No (7. Conversely, if the current density becomes too high,
This is not preferable because OF' itself deteriorates. Furthermore, CF can be applied at either positive or cathodic potential. Reaction time is about 0.1 seconds to about 5 hours. Reaction temperature is about -50U
~T-(10C1 good size t, <&, j, OC~SOC
It will be held in The specific reaction temperature here is selected as appropriate depending on the reactivity temperature used, but it is important to carry out the reaction at a temperature that suppresses thermal polymerization to a negligible level, and avoids excessive thermal polymerization. When performing high-temperature-C, the integrity and uniformity of the resulting composite is impaired. The resulting complex is about 10 to 300C1 [7 or about: (0 to
2007: It can be dried in the temperature range of 2007:.

本発明を実施するに際して用いる溶媒は種々の溶媒を用
いることができるが、その実例と(]てンま水、メタノ
ール、エタノーノベゾロパノール、ブタノールなどのア
ルコール類、アセトン、メチルエチノtクトン、シクロ
ヘキザノンの如きケトン類、酢酸エーブルなどのカルボ
ン酸エステル類、ジメチルホルムアミドの如きカルボン
アミド類を挙げることができる。
Various solvents can be used in carrying out the present invention. Examples include ketones such as zanone, carboxylic acid esters such as acetic acid ester, and carbonamides such as dimethylformamide.

尚、(Fの表面と本発明方法によって施される重合体と
の間の相互作用は、簡単な吸着ない(7は、ファンデル
ワールス力等による物理的な意味における接着を超えた
ものであり、この事実はポリマーの良溶媒で抽出処理1
〜でも多量の未抽出ポリマ〜が認められることから明白
である。
Note that the interaction between the surface of (F) and the polymer applied by the method of the present invention does not involve simple adsorption (7), but is beyond adhesion in the physical sense due to van der Waals forces, etc. , this fact shows that extraction treatment 1 with a good solvent for polymers
This is evident from the fact that a large amount of unextracted polymer is observed even in ~.

次に実施例により、本発明をさらに詳卸1に説明する。Next, the present invention will be further explained in detail with reference to Examples.

実施例1〜2、比較例1〜3 電極ローラー及び、ガイドローラーを配置E〜だ第1図
に示す電解重合装置に、高強gPAN系CP’ロービン
グをセットした後、環式脂肪族系エポキシ化合物として
、ビス(34−エボギシシクロヘギシル)アディベート
50 gr及び支持電解質として硝酸ナトリウム2.5
9r f:D M F 5 (+ 09rに溶解して調
整(〜だ電解反応液を、反応槽(スデンレス製)中にC
Fが浸漬する迄注入した。
Examples 1 to 2, Comparative Examples 1 to 3 Electrode rollers and guide rollers were placed E~ After setting the high-strength gPAN-based CP' roving in the electrolytic polymerization apparatus shown in Figure 1, the cycloaliphatic epoxy compound 50 gr of bis(34-evogycyclohegycyl)adivate and 2.5 gr of sodium nitrate as supporting electrolyte.
9r f: D M F 5 (adjusted by dissolving in +09r).
The injection was continued until F was immersed.

次にCF電位を陽極として、直流変換器を用いて、OF
と電解液間に直流電流を通電(7、室温にて1時間、電
解重合反応を行なった。尚、その際の電流密度は、可変
抵抗器により0.27 A / diになる様に調整し
た。
Next, using the CF potential as an anode and a DC converter, OF
A direct current was passed between the electrolyte and the electrolyte (7. The electrolytic polymerization reaction was carried out at room temperature for 1 hour.The current density at that time was adjusted to 0.27 A/di using a variable resistor. .

反応終了後、生成物をD )A F i’(・て充分洗
浄し7.1、0 (l Cで熱風乾燥して、CFの収束
性及び1嘉測定により、C!F−\のポリマー付着量を
求めた。
After completion of the reaction, the product was thoroughly washed with D)A Fi'(・ and dried with hot air at 7.1,0 (lC), and the polymer of C!F-\ was determined by the convergence of CF and 1. The amount of adhesion was determined.

井グ(前記エボギシ樹脂25 、j9r  とメタクリ
ル酸メチル(M ra A )モノマー 25grの混
合モノマーを使用し/こ場合についても、同様に実施し
た。比較の女めに、通常のビニルモノマーであるM M
 Aモノマー、環式化合物ではない単官能の脂肪族エポ
キシ化合物であるグリシド酸エチル チルの混合物を反応性モノマーとり、て添加した場合の
7tL解沖合挙動についても、同様の重合操作及び重合
後の評価を行い検itt l、た。結果を第1表に示す
。なお部tよすべで重量部を示す。
The same procedure was carried out in this case as well, using a monomer mixture of the above-mentioned Evogishi resin 25, j9r and 25 gr of methyl methacrylate (M ra A ) monomer. M
A similar polymerization operation and post-polymerization evaluation were conducted to determine the 7tL decomposition behavior when a reactive monomer was added to a mixture of monomer A and ethyl methyl glycidate, which is a monofunctional aliphatic epoxy compound that is not a cyclic compound. I did a test. The results are shown in Table 1. In addition, parts t and t indicate parts by weight.

第1表から明らかな様に比較例1.2及び3の場合、O
F’収束性が悪く、ポリマー伺着量が極めて少ないのに
対し、 −C、本発明方法により、CF収束性が、非常
に良好と々ると同時に、ポリマー付着(1%も大[1]
に増大し実用性が飛躍的に向上すること金小し−Cいる
As is clear from Table 1, in the case of Comparative Examples 1.2 and 3, O
While the F' convergence is poor and the amount of polymer adhesion is extremely small, -C, by the method of the present invention, the CF convergence is very good and at the same time polymer adhesion (as much as 1% [1]
It is expected that the amount of metal will be increased and the practicality will be dramatically improved.

第   1   表 1゛・  :  反応性モノ〜−一:cF111−  
: 実施例1.、”l   fi (1部 l  −’  
 l        ’(112311 1I”0部   〃 1 ’J  3:l  2部5部:251 1   ’  
1米2MMA:メタクリル酸メチル 米8 単官能脂肪族エボギシ化合物 CH(Uソl−3−0−02H5 末11  三菱レイヨン@製高強度PAN系CF+5 
  、[)Ml(1: N 、 N−ジメチルホルムア
ミド支持電解質 1 溶 媒::;□ 反 応 牛 成
 物 :■ 硝酸す ( :倒0.1.′ 8 11:    ・    3  ′ i  all  ・、: □ 、・・:・ 夾′     1 ′11 1()I +5  反応条件         米7  CF収束
性  木8実施例 ′J二h1!1例1においで、環式脂肪族エポキシ化合
物(Ll、、−r第ソ表に示し、/ζ化合物を反応性モ
ノマーとL4使Jll l−、たり、外(・、1、全〈
実施例1と同様にして市合う・行ない、Cli”へのボ
リマーイ・1着量を測定計filli I−1′(施I
+l11と[、t lp交1.た結果を第2表い二示゛
j。
Table 1: Reactive mono--1: cF111-
: Example 1. , "l fi (1 part l -'
l' (112311 1I"0 copies 〃 1 'J 3: l 2 parts 5 parts: 251 1'
1 rice 2 MMA: Methyl methacrylate rice 8 Monofunctional aliphatic epoxy compound CH (Usol 1-3-0-02H5 powder 11 Mitsubishi Rayon @ high strength PAN type CF+5
, [) Ml (1: N, N-dimethylformamide supporting electrolyte 1 Solvent::;□ Reaction product: ■ Nitric acid (: 0.1.'8 11: ・3' i all ・,: □ ,...:・ 夾′ 1 ′11 1()I +5 Reaction conditions Rice 7 CF convergence Tree 8 Example 'J2h1!1 In Example 1, a cycloaliphatic epoxy compound (Ll,, -r As shown in Table 1, /ζ compounds can be used with reactive monomers and L4.
The market was carried out in the same manner as in Example 1, and the amount of volume per garment was measured using a measuring meter filli I-1'.
+l11 and [, t lp intersection 1. The results are shown in Table 2.

第2表 1\  反応1シ1士ツマ−、、OF  支寺動子質、
、・溶媒II釘・へν升1゜1    □      
 1 :\ 朱1 原料CF苓: 1. (+ (’1部とした場合
のポリ−7−4′NJ着ら1 未2 人:ビス(3,4−、、−cボキシシク1−1−
\4ンル)アゾ・イベート 米3.  B:2−(a4−エボキシシク目′\ギシノ
l−55−スピロ−3)トーエボキ シ)シクロ−・ギザンーメタージ オキサン * 4.  O: :(、4−−エポギシシクロへギシ
ルメチノl−34−エポギシシクロヘA−リンカルボキ
シレート 末!’+l、):ビニルシクロへギセンジオキザイド第
X2表から明らから様に多官能環式脂肪族エポキシ化合
物[CFへのポリマー伺着量が、いずれも高い水準を示
し、fv。
Table 2.
,・Solvent II Nail・He ν 1゜1 □
1 :\ Vermilion 1 Raw material CF Rin: 1. (+ ('1 part poly-7-4'
\4) Azo Ibate rice 3. B: 2-(a4-Eboxycycline'\Gycinol-55-Spiro-3)To-Eboxy)cyclo-Gyzan-Metadioxane* 4. O: :(,4-epoxycyclohegysylmethino l-34-epoxycycloheyl A-phosphoric carboxylate end!'+l,): Vinylcyclohegycene dioxide As is clear from Table X2, a polyfunctional cycloaliphatic epoxy compound [The amount of polymer adhering to CF was at a high level in all cases, fv.

実施例1〜・5の方法によって得られる重合体組成物約
(1,1Ex−を、円筒口紙と共に秤量し、クロr貝1
ニル−・を抽出溶媒としで、24時間のソックスレ 抽
出試験を行なうことにより、核組酸物の重合体抽出率を
・測定1.た。比較のために、通常の重合触媒により(
7F’ロービング存在下にBu:1.k M合(−て生
成した組成物(比較例4)についても同様の評1i1’
fiをt−Jない横側[7た。結果を第3表に示すが、
比較例に示される組成物中の重合体成分は、24時間の
抽出試験で完全に抽出されるのに対し、本発明方法によ
Qで得られるCF複合体の重合体成分の抽出率は少さく
、大部分は抽出されずにCFに強固に合一化している。
Approximately 1,1Ex- of the polymer composition obtained by the method of Examples 1 to 5 was weighed together with the cylindrical opening paper, and 1
1. Determination of the polymer extraction rate of the nucleic acid by conducting a 24-hour Soxhlet extraction test using Nyl as the extraction solvent. Ta. For comparison, (
Bu:1 in the presence of 7F' roving. Similar evaluations were made regarding the composition (Comparative Example 4) produced by
Fi to t-j side [7]. The results are shown in Table 3.
The polymer component in the composition shown in the comparative example was completely extracted in a 24-hour extraction test, whereas the extraction rate of the polymer component in the CF complex obtained in Q by the method of the present invention was small. However, most of it is not extracted and is strongly integrated into CF.

第   3   表 :   \ 1゛\ □ \ \ I  ゝ 11JaiflJ ■ 1 −− 1〃 2 − I。Table 3 :  \ 1゛\ □ \ \ Iゝ 11 JaiflJ ■ 1 --- 1〃 2 − I.

3 1′4 :〃 5 −−− j上し中交例 1    4 来1.原料OFを100部とした場合のポリマー伺着惜
実施例6 CFの種類を変えた以外は、実施例1と同様にして反応
を実施し、得られた組成物を評価した結果を第4表に示
す。
3 1'4 :〃 5 --- jUpper Interchange Example 1 4 Next 1. Example 6: Poor polymer adhesion when raw material OF was 100 parts Table 4 shows the results of evaluating the obtained composition by carrying out the reaction in the same manner as in Example 1 except for changing the type of CF. Shown below.

第   4   表 来1 電W(重合条件 CF:0.123部、硝酸ナトリウム:2.5部( ERL−4299:50部、DMF:500部第4表か
ら明らかな様に、本発明方法は、重合活性に関するCF
選択性が認められず、概ねポリマー付着量は、良好であ
ると共に一生成復合体中の重合体成分の抽出率は小さく
、大部分は抽出され、ず、OFと強固に合一化している
ことがわかる。
Part 4 Table 1 Electron W (polymerization conditions CF: 0.123 parts, sodium nitrate: 2.5 parts (ERL-4299: 50 parts, DMF: 500 parts) As is clear from Table 4, the method of the present invention CF regarding polymerization activity
No selectivity was observed, and the amount of polymer deposited was generally good, and the extraction rate of the polymer component in the one-produced polymer was small, and most of it was not extracted, but was strongly combined with OF. I understand.

実施例7 環式脂肪族エポキシ化合物との共反応性モノマーとして
、MMAのかわりに第5表に示・J゛反応性モノマーを
使用する以外は実施例2と同様に反応し、得られた組成
物を評価した結果を第5表に示ずO 第   5   表 *:1 8T : スチレンモノマー 米2  丁(u、A:  アクリル酸n−]゛チルエス
テル米a  MAA:  メタクリル酸 14   GMA:  グリシジルメタクリレート、重
量比は5 (1150釆5   HDU:  1.6−
Hoxamethylene  cLiethylen
eurea来6  AZM  :  2−(1−azi
ridiny:1−)ethy’Lme1;hacry
lat。
Example 7 The reaction was carried out in the same manner as in Example 2, except that the reactive monomer shown in Table 5 was used instead of MMA as the co-reactive monomer with the cycloaliphatic epoxy compound, and the resulting composition The results of the evaluation are not shown in Table 5. Table 5 *: 1 8T: Styrene monomer rice 2 tons (u, A: Acrylic acid n-]゛thyl ester rice a MAA: Methacrylic acid 14 GMA: Glycidyl methacrylate, The weight ratio is 5 (1150 pots 5 HDU: 1.6-
Hoxamethylene cLiethylen
From eurea 6 AZM: 2-(1-azi
ridiny:1-)ethy'Lme1;hacry
lat.

TDEI :  2 、4−Dietlylurea、
toluidineTAZO:   Tetramet
hylolmethane  −tr土 −β −−a
ziridinylpropyonateH2 / 原料OFを100部とした場合のポリマーtJ着量 第f)表から明らか乃様に、本発明に用いられる共反応
t+十ツマ−と[7てVよ、通常のラジカル重合し、5
うるビ?1 )1単址休及びアジリジン環含有化合物r
1、いずれも適用できることがわかる。
TDEI: 2, 4-Dietlylurea,
toluidineTAZO: Tetramet
hylolmethane -tr soil -β --a
ziridinylpropyonate H2 / Polymer tJ coverage when the raw material OF is 100 parts.
Urubi? 1) Compound containing 1 moiety and aziridine ring
1. It can be seen that both are applicable.

実施例8 支4’3電解質とし2て硝酸ツートリウム2509r 
を脱・イ」ン水!二i 00 gr 中に溶解17た溶
液にPAN糸(! g゛(−三菱レイ1ン製HT )ロ
ービング0.123、Q+−を・浸漬I27、充分乾燥
[7た後、実施例1と同様にドツトさ1また反応器を用
いて、該処理OF全11゛を、あらかじめ調整した反応
液(ERL−429+、1を1)MF5(If−1,9
r−中に溶解(7た溶液)中に浸漬(−だ。
Example 8 Zutrium nitrate 2509r as support 4'3 electrolyte
Take off the water! Two PAN threads (Mitsubishi Ray 1 HT) roving 0.123, Q+- were dipped in a solution of 17% dissolved in 100 gr. After being thoroughly dried [7], the same method as in Example 1 was carried out. Also, using a reactor, add the previously prepared reaction solution (ERL-429+, 1 to 1) MF5 (If-1,9
Dissolved in r- (7 solution) immersed in (-d).

次にCI[i″屯缶陽極と[7て、直流変換器を用いて
該処理(])゛と反応液間に直流電流を通電し、宰温に
て1時間、電解重合反応を行なった。
Next, a direct current was passed between the treatment ()'' and the reaction liquid using the CI [i'' tube anode and a DC converter, and an electrolytic polymerization reaction was carried out for 1 hour at room temperature. .

尚、その際の電流密度は、可変抵抗器により、0、27
 A / can?になる様に調整した。重合終了後、
実施例1と同様に評価;〜た結W7、OFへのポリマー
伺着量i、、t、 8 t、を部であり、しかも得られ
た複合体は、CF表面を該反応性モノマーの重合体にて
、(リ−に、かつ)強固に固着化された組成物てあ−)
だ。
In addition, the current density at that time is set to 0, 27 by a variable resistor.
A/Can? I adjusted it so that After polymerization,
Evaluation was made in the same manner as in Example 1; W7, the amount of polymer adhering to the OF was i, t, 8 t, and the resulting composite had the CF surface covered with the weight of the reactive monomer. When combined, the composition is firmly and firmly fixed.
is.

実施例を(。Examples (.

本発明によって得られる市7合体組成物を用いてビスフ
ェノールAタイプ汎FI# =1’−ボーVシ樹脂との
複合体(tlni、d、1rectiona、−1Ca
rdpoal、fo ) f作製し、賦型物のストラン
ド強度、層間剪断強度及び曲げ強度等の機械的特性を評
価1〜だ。比較のために、車処理のOF(表中単純ブし
・ンドと(7て示す)を同様に複合化して評価を行なっ
た。
Bisphenol A type pan-FI# = 1'-Beau V resin complex (tlni, d, 1 rectiona, -1 Ca
rdpool, fo ) f was prepared, and the mechanical properties of the shaped product, such as strand strength, interlaminar shear strength, and bending strength, were evaluated as 1 to 1. For comparison, the OF of car processing (simple block/end (indicated by 7) in the table) was similarly combined and evaluated.

結IJを第6表に示す。The resulting IJ is shown in Table 6.

第   6   表 I     機 械  的  特  性    :来1
 0F含有率60 VOI % Hr、 (H表から明らかな様に、本発明方法による重
合体組成物は機械的特性等の実用性にお・い−C1優れ
プζ組成物であることを示している。
Table 6 Mechanical properties: 1
0F content 60 VOI % Hr, (As is clear from the table H, the polymer composition produced by the method of the present invention has excellent mechanical properties and other practical properties. There is.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明によるCFロー)ピンク゛・\の電解重
合装置の一実施態様を示す説明図である。 符−弓の説明 (j)  ・・・ 電極j’l −ラー(銅製)■ ・
・・ ガイ1釦−ラー(ガラス製)■ ・・・ OF 
UJ −ピング ■ ・−・ 竜角イ重合液 (の ・・ 反応槽(ステンレ′ス製)(の ・・・ 
直流変換器 ■ ・・・ 可変抵抗器 ■ ・・・ 電流語 特¥r出願人 三菱レイヨン株式会社 代理人 弁理−に 1)村 武 散 策1図 / ■  れ°1.  補  正  内 ()5式 )昭和
5ε3 fi−4月/枳11 t8i rF I’t’ f−<官  オー  杉  
相  夫  1〆ひ1 、 Fli (iの表出 11(1和57 ’I Q、X■i+′l願第2266
52’>シン3餓明σ)名Y11 ?Ii f1!、!中合体組成物の製造法コ3.浦11
−4りる者 =Ij (’lどの関係 特九′1出願人東京都中央E
メ京橋イJ l」3番19号(60、’3 )閣菱しイ
F−1ン株式会r(取締1ジ拐 fぐ    金  澤
  脩  二lI 、代理 人 東5バfillン艮区虎、)閂−二1L18番1″I″
)]111和5 B 3T33jl 29 に!イNJ
ざt送6 、  ン+li  il  の ス・1 象
                         
       −9明■1μmの浄11((内容に変更
なし)  パl実施例 実施例1において、環式脂肪族エポギシ化合物と17で
第2表に示した化合物を反応性モノマーとj、2てl1
i74 Jfi t、メこ以外は、全〈実施例1と同様
にして取合全行ない、CFへのポリマー付着贋を測定評
価1〜、実施例1と比較した結果を第2表に示す。 第2表 第3表 *1 厚相CFを100部とした場合のポリマー利着量
実施例6゜ CFの種類を変乏−た以外は、実施例1と同様に[7て
反応を実施し、得られた組成物をRf’価した結果f:
第4喪に示す。 第4表 十lil讐7角1 i(j 合イミ子牛CF : 0.
123部、硝酸ナトリウム:2.5部( ElえL−4299:50部、DMF : 500部第
4表から明らかな様に、本発明方法ンま、重合活4′1
に閏]るCF選択性が望められず、概ねポリ=7−イ・
1γIF IS目−11、良好であると共に、生成複合
体中*I  ST  :スチレンモノマー *2BuAニアクリル酸n−ブチルニスプル*3MAA
:メタクリル酸 *4  GMA ニゲリシジルメタクリレート、重量比
は50150$5  Hl)U : L6− Hexa
methy!ene  dlet、hyleneure
a均−に、かつ強固に固着化された組成物であった。 実施例9゜ 本発明によって得られる重合体組成物を用いてビスフェ
ノールAタイプ汎用エポキシ樹脂との複合体(Unld
irectional Composlte )を作製
し、賦型物のストランド強度、層間剪断強度及び曲げ強
度等の機械的特性を評価した。比較のために、未処理の
CF(表中単純ブレンドとして示す)を同様に複合化し
て評価を行なった。 結果を第6表に示す。 第6表 *I  CF金含有率0Vo1% −I損−
FIG. 1 is an explanatory diagram showing an embodiment of an electrolytic polymerization apparatus for CF raw material according to the present invention. Sign - Explanation of bow (j) ・・・ Electrode j'l - Ra (copper)■ ・
・・ Guy 1 button - ra (made of glass) ■ ・・・ OF
UJ-Ping ■ - Ryukakui polymerization solution (... Reaction tank (stainless steel) (...
DC converter ■ ... Variable resistor ■ ... Current language special ¥r Applicant Mitsubishi Rayon Co., Ltd. Agent Patent attorney 1) Takeshi Mura Stroll 1 Figure / ■ Re°1. Correction () 5 formula) Showa 5ε3 fi-April/枳11 t8i rF I't'f-<Government O Cedar
Aifu 1〆hi1, Fli (Expression 11 of i (1 sum 57 'I Q, X■i+'l application No. 2266
52'> Shin 3 Hangmei σ) Name Y11? Ii f1! ,! Production method of intermediate composition 3. Ura 11
-4 Rir person = Ij ('l Which relationship Special 9'1 Applicant Tokyo Chuo E
Mekyobashii Jl'' 3 No. 19 (60, '3) Kakubishi Shiin F-1 stock company r (enforcement 1st kidnapping fgu) Osamu Kanazawa 2lI, agent Nito 5 Bafilln Aiku Tora ,) Bolt-2 1L No. 18 1″I″
)] 111 sum 5 B 3T33jl 29 to! Lee NJ
Zatsu 6, N+li il's S・1 Elephant
-9 bright ■ 1 μm filter 11 ((no change in content) Pal Example In Example 1, a cycloaliphatic epoxy compound and the compound shown in Table 2 in 17 were combined with a reactive monomer, j, 2 and l1
The entire assembly was carried out in the same manner as in Example 1, except for the i74 Jfit and the mechanism. Table 2 shows the results of measurement and evaluation of polymer adhesion to CF from Evaluation 1 to Example 1. Table 2 Table 3 *1 Amount of polymer gain when thick phase CF is 100 parts Example 6゜The reaction was carried out in the same manner as in Example 1 except that the type of CF was changed. The result of Rf' rating of the obtained composition f:
It is shown in the fourth mourning. Table 4: 7 points 1 i (j total calf CF: 0.
123 parts, sodium nitrate: 2.5 parts (Ele L-4299: 50 parts, DMF: 500 parts As is clear from Table 4, the polymerization activity of the method of the present invention was 4'1.
CF selectivity cannot be expected, and poly=7-i.
1γIF IS order -11, good and in the produced complex *I ST: Styrene monomer *2 BuA n-butyl acrylate *3 MAA
:Methacrylic acid*4 GMA nigericidyl methacrylate, weight ratio is 50150$5 Hl)U : L6- Hexa
Methy! ene dlet, hyleneure
The composition was evenly and firmly fixed. Example 9 A composite with bisphenol A type general-purpose epoxy resin (Unld
A directional composite was prepared, and mechanical properties such as strand strength, interlaminar shear strength, and bending strength of the shaped product were evaluated. For comparison, untreated CF (shown as a simple blend in the table) was similarly composited and evaluated. The results are shown in Table 6. Table 6 *I CF gold content 0Vo1% -I loss-

Claims (2)

【特許請求の範囲】[Claims] (1)  炭素繊維を電極として、反応性子ツマ−を電
解重合するにあたり、環式脂肪族系エポキシ化合物を、
反応性モノマーの一部捷たは全部として添加することを
特徴とする炭素繊維とエポキシ重合体が、強固に合一化
された重合体組成物の製造法。
(1) When electrolytically polymerizing a reactive polymer using carbon fiber as an electrode, a cycloaliphatic epoxy compound is
1. A method for producing a polymer composition in which carbon fiber and epoxy polymer are strongly integrated, characterized by adding the reactive monomer as part or all of the reactive monomer.
(2)環式脂肪族系エポキシ化合物が下記の一般戊C+
) (式中R1は七〜o −!−r(3−f RsHC+ 
〜C21の〕′ル:Vレン基を示−す。R2は04−(
3Qのアルキレン基を示す。) 又は一般式(1) (式中R4は030以下のアルキレン基を示す。)で表
わされる環式脂肪族系エポキシ化合物である特許請求の
範囲第1項記載の重合体組成物の製造法。
(2) The cycloaliphatic epoxy compound is the following general C+
) (In the formula, R1 is 7~o -!-r(3-f RsHC+
~C21]': represents a V ren group. R2 is 04-(
Indicates the alkylene group of 3Q. ) or a cycloaliphatic epoxy compound represented by general formula (1) (wherein R4 represents an alkylene group of 030 or less), the method for producing a polymer composition according to claim 1.
JP22665282A 1982-10-19 1982-12-27 Production of new polymer composition Granted JPS59120620A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP22665282A JPS59120620A (en) 1982-12-27 1982-12-27 Production of new polymer composition
EP83110347A EP0106352B1 (en) 1982-10-19 1983-10-17 Novel polymer composition
DE8383110347T DE3380065D1 (en) 1982-10-19 1983-10-17 Novel polymer composition
US06/542,950 US4510024A (en) 1982-10-19 1983-10-18 Novel polymer composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22665282A JPS59120620A (en) 1982-12-27 1982-12-27 Production of new polymer composition

Publications (2)

Publication Number Publication Date
JPS59120620A true JPS59120620A (en) 1984-07-12
JPH0145490B2 JPH0145490B2 (en) 1989-10-03

Family

ID=16848532

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22665282A Granted JPS59120620A (en) 1982-10-19 1982-12-27 Production of new polymer composition

Country Status (1)

Country Link
JP (1) JPS59120620A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0247365A (en) * 1988-08-05 1990-02-16 Toshiba Ceramics Co Ltd Surface-treatment of formed carbon fiber

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0247365A (en) * 1988-08-05 1990-02-16 Toshiba Ceramics Co Ltd Surface-treatment of formed carbon fiber

Also Published As

Publication number Publication date
JPH0145490B2 (en) 1989-10-03

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