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JPH0414844B2 - - Google Patents
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JPH0414844B2 - - Google Patents

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Publication number
JPH0414844B2
JPH0414844B2 JP61195177A JP19517786A JPH0414844B2 JP H0414844 B2 JPH0414844 B2 JP H0414844B2 JP 61195177 A JP61195177 A JP 61195177A JP 19517786 A JP19517786 A JP 19517786A JP H0414844 B2 JPH0414844 B2 JP H0414844B2
Authority
JP
Japan
Prior art keywords
fibers
conductive
resin composition
conductive resin
producing
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.)
Expired - Lifetime
Application number
JP61195177A
Other languages
Japanese (ja)
Other versions
JPS6351109A (en
Inventor
Hidehiro Iwase
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.)
Toshiba Chemical Products Co Ltd
Original Assignee
Toshiba Chemical Products 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 Toshiba Chemical Products Co Ltd filed Critical Toshiba Chemical Products Co Ltd
Priority to JP19517786A priority Critical patent/JPS6351109A/en
Publication of JPS6351109A publication Critical patent/JPS6351109A/en
Publication of JPH0414844B2 publication Critical patent/JPH0414844B2/ja
Granted legal-status Critical Current

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  • Reinforced Plastic Materials (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

[発明の目的] (産業上の利用分野) 本発明は、導電性繊維の分散性がよく、繊維充
填率が少なくてすみ、かつ成形品の導電性に優れ
た導電性樹脂組成物の製造方法に関する。 (従来の技術) 従来、多数のフイラメントからなる導電性繊維
を熱可塑性樹脂に充填分散させて導電性樹脂組成
物とする場合、まず、特公昭60−54967号公報に
示されているように金属繊維を熱可塑性樹脂の溶
液やエマルジヨンの収束剤を用いて収束し、これ
を1〜15mmの長さに切断し、次に、この切断した
収束繊維を熱可塑性プラスチツクに混合し、押出
機で混練分散して導電性プラスチツクとする。さ
らに、特開昭58−129031号公報に示されているよ
うに上記混練分散した導電性プラスチツクを射出
成形しやすいようにペレタイザーで切断してペレ
ツト化していた。 しかしながら、上記従来の導電性樹脂組成物
は、前段の混練分散工程において押出機の加熱シ
リンダー内部で金属繊維を混練分散させるため、
繊維が切れやすい欠点がある。また、後段のペレ
ツト化工程では、再度ペレツト化の切断をしてい
るため、更に繊維が切断され、当初の繊維長さよ
りはるかに短くなる欠点があつた。そしてまた、
従来の導電性樹脂組成物を使用して成形品とした
場合、導電性が経時変化と共に低下したり、所望
の導電性が得られないことから、導電性繊維の充
填量を多くする必要があり、その結果、成形品の
成形性、物性を阻害し、またコスト高となり問題
となつていた。 (発明が解決しようとする問題点) 本発明は、上記従来導電性樹脂組成物の欠点を
解消するためになされたもので、導電性繊維の分
散性がよく、低い繊維充填率であつても導電性に
優れ、しかも樹脂の物性を損ねることの少ない導
電性樹脂組成物の製造方法を提供しようとするも
のである。 [発明の構成] (問題点を解決するための手段と作用) 本発明は、上記の目的を達成するため鋭意研究
を重ねた結果、繊維を切断し、導電性を損ねる主
たる原因となる熱可塑性樹脂と導電性繊維との押
出機による混練分散工程を省くとともに、収束剤
に化学発泡剤を用いることによつて、射出成形に
おいて熱可塑性樹脂への導電性繊維の分散性がよ
く、低い繊維充填率で導電性に優れ、かつ成形品
の物性を損ねることの少ないことを見いだし、本
発明を完成するに至つたものである。すなわち、
本発明は、熱可塑性樹脂および化学発泡剤を含む
収束剤を溶剤に溶解し、該収束剤に導電性繊維を
浸漬収束し、乾燥して溶剤を揮散させた後、ペレ
ツト状に切断することを特徴とする導電性樹脂組
成物の製造方法である。 本発明に用いる導電性繊維としては、ステンレ
ス繊維、アルミニウム繊維、銅繊維、炭素繊維又
は表面に金属メツキ層を有する炭素繊維、ガラス
繊維若しくは有機繊維が挙げられ、これらは単独
又は2種以上混合して使用することができる。収
束剤で収束される導電性繊維のフイラメント数
は、500〜20000本程度が適当である。 本発明に用いる収束剤は、熱可塑性樹脂および
化学発泡剤を含むものである。ここで用いる熱可
塑性樹脂としては、塩化ビニル樹脂、エチレンビ
ニルアセテート樹脂、ポリスチレン樹脂、AS樹
脂、ABS樹脂、ポリエチレン樹脂、ポリプロピ
レン樹脂、ポリエチレンテレフタレート樹脂、ポ
リブチレンテレフタレート樹脂、ナイロン樹脂、
ポリカーボネート樹脂、変性ポリフエニレンオキ
サイド樹脂、ポリフエニレンサルフアイド樹脂、
ポリエーテルサルホン樹脂、ポリエーテルイミド
樹脂等が挙げられ、これは単独又は、2種以上混
合して使用する。また化学発泡剤としては、アゾ
ジカルボンアミド(ADCA)、アゾビスイソブチ
ロニトリル(AIBN)、4,4′−オキシビスベン
ゼンスルホニルヒドラジツド(OBSH)、N,
N′−ジニトリロペンタメチレンテトラミン
(DPT)、p−トルエンスルホニルセミカルバジ
ツド(TSSC)、p−トルエンスルホニルヒドラ
ジツド(TSH)、トリヒドラゾトリアジン
(THT)等が挙げられ、これらは単独又は、2
種以上混合して使用される。また、これらの化学
発泡剤に必要に応じて発泡助剤を添加し、発泡温
度、ガスを調整したものを使用することもでき
る。発泡助剤としては、亜鉛華、三塩基性硫酸
鉛、白艷華などの無機塩、ステアリン酸亜鉛、ス
テアリン酸鉛などの金属石鹸、尿素化合物等が挙
げられ、これらは単独又は、2種以上混合して使
用される。また熱可塑性樹脂に化学発泡剤を予め
加えたものが市販されており、それらを加えても
よい。 化学発泡剤は、収束剤に含まれる熱可塑性樹脂
に対して2〜30重量%配合することが望ましい。
配合割合が2重量%未満では、発泡ガス圧が不足
し導電性繊維の分散が悪く好ましくない。また30
重量%を超えると成形品そのものが発泡成形品と
なり、通常の成形品としては好ましくない。 導電性繊維を収束剤で被覆収束させる方法とし
ては、特に制限はされなく、いずれの方法でもよ
いが、収束剤を塩化メチレン、テトラクロロエタ
ン、ベンゼン、クロロホルム等の溶剤に溶解し、
この溶液中に導電性繊維を浸漬する方法や、収束
剤を加熱溶融し、押出機から押し出すと同時に押
出機ダイス中心に連続した導電性繊維を通すこと
によつて導電性繊維を収束剤で被覆収束する方法
などが好ましく採用される。収束剤の付着量は、
導電性繊維に対して、5〜40重量%であることが
望ましく、5重量%未満では発泡圧が不足して分
散性が悪く、また40重量%を超えると、熱可塑性
樹脂の物性を損ない好ましくない。導電性繊維を
こうして収束剤で被覆収束し、冷却後、ペレツト
状に切断して導電性樹脂組成物を得る。このペレ
ツトの長さは、3〜12mmが望ましく、長さが3mm
未満では導電性が低く、また12mmを超えると導電
性繊維の分散性が悪く、更に成形する際に格子状
部分等、成形品細部に導電性繊維が充填されず好
ましくない。 導電性繊維を加熱溶融した収束剤で押出被覆収
束する方法は、マトリツクスの熱可塑性樹脂が耐
溶剤性の優れた例えばポリエチレンテレフタレー
ト、ポリブチレンテレフタレート、ナイロン等で
ある場合、一般に溶剤では溶けにくく、極性の強
い溶剤を使用しなければならないので、これらの
溶剤を使用しない方法として有用である。押出被
覆収束後、偏平に加圧して導電性繊維を分散さ
せ、ペレツト状に切断して導電性樹脂組成物とす
る。これをそのまま成形材料とするか、またはこ
のペレツト状に切断したものをマスターペレツト
とし、これに熱可塑性樹脂からなるナチユラルペ
レツトを配合して成形材料として使用することも
できる。また化学発泡剤が配合された熱可塑性樹
脂には、例えばエンジニアプラスチツク社製商品
名、FCJ−110(ノリル用)、FVC−60/65(PBT
用)や永和化成工業社製商品名、ポリスレンE1
06,105,201等がある。これらは単独又
は2種以上混合して使用することができる。 収束剤中又はナチユラルペレツト中に含まれる
化学発泡剤によつて、射出成形機シリンダー中で
加熱され、化学発泡剤が分解し、窒素ガスや炭酸
ガスを発生して発泡し、そのガス圧力を利用して
導電性繊維を分散させ、さらに射出成形機によつ
て分散混練させるものである。従つて射出成形機
による導電性繊維の切断は少なく、よく分散し、
かつ導電性に優れた成形品を得ることができる。 (実施例) 次に本発明を実施例によつて具体的に説明する
が、本発明はこれらの実施例によつて限定される
ものではない。以下の実施例及び比較例において
「%」とは「重量%」を意味する。 実施例 1 熱可塑性樹脂TFX−410(三菱モンサント化学
社製ABS樹脂、商品名)に対して化学発泡剤ア
ゾジカルボンアミド(ADCA)を3%添加し、
これを2倍量の塩化メチレンによく撹拌して収束
剤とした。この溶液にニツケルメツキ層を有する
炭素繊維(直径8μm、フイラメント数12000本)
を通過させ、次いで乾燥して溶剤を揮散させた。
この時のABS樹脂、ニツケルメツキ層を有する
炭素繊維、ADCAの割合は、重量比で67.9%、30
%、2.1%であつた。これを6mmのペレツト状に
切断して導電性樹脂組成物を得た。この組成物を
用いて射出成形を行い、成形品を得た。成形品の
X線撮影を行い、ニツケルメツキ層を有する炭素
繊維の分散性の評価と、導電性を試験したので第
1表に示したが、本発明の優れた効果が確認され
た。 比較例 1 熱可塑性樹脂ABS樹脂を塩化メチレンに溶解
した溶液中にニツケルメツキ層を有する炭素繊維
(直径8μm、フイラメント数12000本)を通過さ
せ、次いで乾燥して溶剤を揮散させた。このとき
のABS樹脂、ニツケルメツキ層を有する炭素繊
維の割合は、70%、30%であつた。これを長さ6
mmのペレツト状に切断して導電性樹脂組成物を得
た。この組成物を用いて射出成形を行い成形品を
得た。この成形品について実施例と同様に試験を
行い結果を得たので、第1表に示した。
[Objective of the invention] (Industrial application field) The present invention provides a method for producing a conductive resin composition that has good dispersibility of conductive fibers, requires a small fiber filling rate, and has excellent conductivity of molded products. Regarding. (Prior Art) Conventionally, when preparing a conductive resin composition by filling and dispersing conductive fibers consisting of a large number of filaments in a thermoplastic resin, first, as shown in Japanese Patent Publication No. 60-54967, metal The fibers are converged using a thermoplastic resin solution or emulsion convergence agent, and then cut into lengths of 1 to 15 mm.Then, the cut convergent fibers are mixed with thermoplastic plastic and kneaded using an extruder. Disperse to make conductive plastic. Further, as disclosed in Japanese Patent Application Laid-Open No. 129031/1982, the kneaded and dispersed conductive plastic was cut into pellets using a pelletizer to facilitate injection molding. However, in the above conventional conductive resin composition, the metal fibers are kneaded and dispersed inside the heating cylinder of the extruder in the previous kneading and dispersion step.
The disadvantage is that the fibers are easy to break. In addition, in the subsequent pelletizing step, the pelletizing process is again cut, resulting in further cutting of the fibers, which has the disadvantage that the length of the fibers becomes much shorter than the initial length. and again,
When molded products are made using conventional conductive resin compositions, the conductivity decreases over time or the desired conductivity cannot be obtained, so it is necessary to increase the amount of conductive fibers filled. As a result, the moldability and physical properties of the molded product are impaired, and the cost is increased, which has become a problem. (Problems to be Solved by the Invention) The present invention has been made to eliminate the drawbacks of the conventional conductive resin compositions described above, and has good dispersibility of conductive fibers, even at a low fiber filling rate. The object of the present invention is to provide a method for producing a conductive resin composition that has excellent conductivity and does not impair the physical properties of the resin. [Structure of the Invention] (Means and Effects for Solving the Problems) As a result of extensive research to achieve the above object, the present invention has been developed to solve the problem of thermoplastic fibers, which is the main cause of cutting fibers and impairing conductivity. By omitting the kneading and dispersion process of the resin and conductive fibers using an extruder, and by using a chemical foaming agent as a sizing agent, the conductive fibers have good dispersibility in the thermoplastic resin during injection molding, resulting in low fiber filling. The present invention was completed based on the discovery that the material has excellent conductivity and does not impair the physical properties of the molded product. That is,
The present invention involves dissolving a binding agent containing a thermoplastic resin and a chemical foaming agent in a solvent, immersing conductive fibers in the binding agent, converging them, drying them to volatilize the solvent, and then cutting them into pellets. This is a characteristic method for producing a conductive resin composition. The conductive fibers used in the present invention include stainless steel fibers, aluminum fibers, copper fibers, carbon fibers, carbon fibers having a metal plating layer on the surface, glass fibers, and organic fibers, which may be used alone or in combination of two or more. can be used. The appropriate number of filaments of the conductive fibers to be converged with the convergent agent is about 500 to 20,000. The sizing agent used in the present invention contains a thermoplastic resin and a chemical blowing agent. The thermoplastic resins used here include vinyl chloride resin, ethylene vinyl acetate resin, polystyrene resin, AS resin, ABS resin, polyethylene resin, polypropylene resin, polyethylene terephthalate resin, polybutylene terephthalate resin, nylon resin,
Polycarbonate resin, modified polyphenylene oxide resin, polyphenylene sulfide resin,
Examples include polyether sulfone resin and polyetherimide resin, which may be used alone or in combination of two or more. Chemical blowing agents include azodicarbonamide (ADCA), azobisisobutyronitrile (AIBN), 4,4'-oxybisbenzenesulfonylhydrazide (OBSH), N,
Examples include N'-dinitrilopentamethylenetetramine (DPT), p-toluenesulfonyl semicarbazide (TSSC), p-toluenesulfonylhydrazide (TSH), trihydrazotriazine (THT), etc. Or 2
Used as a mixture of more than one species. Further, it is also possible to use a chemical foaming agent in which a foaming aid is added to these chemical foaming agents as necessary, and the foaming temperature and gas are adjusted. Examples of foaming aids include inorganic salts such as zinc white, tribasic lead sulfate, and white sulfur, metal soaps such as zinc stearate and lead stearate, and urea compounds, which may be used alone or in combination of two or more. used. Furthermore, thermoplastic resins prepared by adding chemical blowing agents in advance are commercially available, and these may also be added. It is desirable that the chemical blowing agent be blended in an amount of 2 to 30% by weight based on the thermoplastic resin contained in the sizing agent.
If the blending ratio is less than 2% by weight, the foaming gas pressure will be insufficient and the conductive fibers will be poorly dispersed, which is not preferable. 30 again
If it exceeds % by weight, the molded product itself becomes a foamed molded product, which is not preferable as a normal molded product. The method of coating and converging the conductive fibers with a sizing agent is not particularly limited and any method may be used, but the sizing agent may be dissolved in a solvent such as methylene chloride, tetrachloroethane, benzene, chloroform, etc.
The conductive fibers can be coated with a binding agent by dipping the conductive fibers in this solution, or by heating and melting the binding agent, extruding it from the extruder, and simultaneously passing a continuous conductive fiber through the center of the extruder die. A method that converges is preferably adopted. The amount of adhesion agent is
It is desirable that the amount is 5 to 40% by weight based on the conductive fibers; if it is less than 5% by weight, the foaming pressure will be insufficient and the dispersibility will be poor, and if it exceeds 40% by weight, the physical properties of the thermoplastic resin will be impaired. do not have. The conductive fibers are thus coated and converged with a binding agent, cooled, and then cut into pellets to obtain a conductive resin composition. The length of this pellet is preferably 3 to 12 mm, and the length is 3 mm.
If it is less than 12 mm, the conductivity will be low, and if it exceeds 12 mm, the dispersibility of the conductive fibers will be poor, and furthermore, during molding, the conductive fibers will not be filled into the details of the molded product, such as lattice parts, which is not preferable. When the thermoplastic resin of the matrix is made of polyethylene terephthalate, polybutylene terephthalate, nylon, etc., which has excellent solvent resistance, it is generally difficult to dissolve in solvents and is polar. This method is useful as a method that does not use strong solvents. After the extrusion coating is completed, the conductive fibers are dispersed by applying pressure flatly, and the conductive fibers are cut into pellets to obtain a conductive resin composition. This can be used as a molding material as it is, or it can be cut into pellets and used as a master pellet, and natural pellets made of thermoplastic resin can be blended therein and used as a molding material. In addition, thermoplastic resins containing chemical blowing agents include, for example, the product name manufactured by Engineer Plastics, FCJ-110 (for Noryl), FVC-60/65 (PBT
) and Eiwa Kasei Kogyo Co., Ltd. product name, polystyrene E1
There are 06, 105, 201, etc. These can be used alone or in combination of two or more. The chemical blowing agent contained in the sizing agent or natural pellets is heated in the cylinder of the injection molding machine, the chemical blowing agent decomposes, generates nitrogen gas and carbon dioxide gas, and foams, reducing the gas pressure. The conductive fibers are then dispersed using the injection molding machine and then dispersed and kneaded using an injection molding machine. Therefore, the conductive fibers are not cut by the injection molding machine and are well dispersed.
Moreover, a molded article with excellent conductivity can be obtained. (Examples) Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these Examples. In the following Examples and Comparative Examples, "%" means "% by weight". Example 1 3% of a chemical blowing agent azodicarbonamide (ADCA) was added to thermoplastic resin TFX-410 (ABS resin manufactured by Mitsubishi Monsanto Chemical Co., Ltd., trade name),
This was thoroughly stirred in twice the amount of methylene chloride to obtain a sizing agent. Carbon fiber with a nickel-metal layer in this solution (8 μm in diameter, 12,000 filaments)
was passed through and then dried to evaporate the solvent.
At this time, the proportion of ABS resin, carbon fiber with nickel plating layer, and ADCA was 67.9% by weight, 30
%, 2.1%. This was cut into 6 mm pellets to obtain a conductive resin composition. Injection molding was performed using this composition to obtain a molded article. The molded product was photographed by X-rays, and the dispersibility of the carbon fibers having a nickel plating layer was evaluated and the conductivity was tested, as shown in Table 1, and the excellent effects of the present invention were confirmed. Comparative Example 1 A carbon fiber (8 μm in diameter, 12,000 filaments) having a nickel plating layer was passed through a solution in which a thermoplastic ABS resin was dissolved in methylene chloride, and then dried to volatilize the solvent. At this time, the proportions of ABS resin and carbon fiber having a nickel plating layer were 70% and 30%. Make this length 6
A conductive resin composition was obtained by cutting into pellets of mm size. Injection molding was performed using this composition to obtain a molded article. This molded article was tested in the same manner as in the examples, and the results are shown in Table 1.

【表】【table】

【表】 評価した。○印は良好、×印は不良。
[発明の効果] 以上の説明および第1表から明らかなように、
本発明の導電性樹脂組成物の製造方法は、その繊
維収束剤に化学発泡剤を使用することによつて、
熱可塑性樹脂と導電性繊維との分散に押出機によ
る混練分散工程を必要とせず、その結果長い導電
性繊維を少なく充填できることとなるために、導
電性が優れかつマトリツクス樹脂の特性を損なう
ことのない導電性樹脂組成物が得られる。従つ
て、本発明の導電性樹脂組成物の製造方法を使用
することによつて信頼性の高い電子機器の成形品
を得ることができる。
[Table] Evaluated. ○ mark is good, × mark is bad.
[Effect of the invention] As is clear from the above explanation and Table 1,
The method for producing the conductive resin composition of the present invention uses a chemical blowing agent as the fiber binding agent,
There is no need for a kneading and dispersion process using an extruder to disperse the thermoplastic resin and conductive fibers, and as a result, fewer long conductive fibers can be filled, resulting in excellent conductivity and without damaging the properties of the matrix resin. An electrically conductive resin composition with no oxidation can be obtained. Therefore, by using the method for producing a conductive resin composition of the present invention, a highly reliable molded article of electronic equipment can be obtained.

Claims (1)

【特許請求の範囲】 1 熱可塑性樹脂および化学発泡剤を含む収束剤
を溶剤に溶解し、該収束剤に導電性繊維を浸漬収
束し、乾燥して溶剤を揮散させた後、ペレツト状
に切断することを特徴とする導電性樹脂組成物の
製造方法。 2 導電性繊維が、ステンレス繊維、アルミニウ
ム繊維、銅繊維、炭素繊維又は表面に金属メツキ
層を有する炭素繊維、ガラス繊維若しくは有機繊
維である特許請求の範囲第1項記載の導電性樹脂
組成物の製造方法。 3 収束剤で被覆収束された導電性繊維数が、
500〜20000本である特許請求の範囲第1項又は第
2項記載の導電性樹脂組成物の製造方法。 4 化学発泡剤が、アゾジカルボンアミド、アゾ
ビスイソブチロニトリル、4,4′−オキシビス
ベンゼンスルホニルヒドラジツド、p−トルエン
スルホニルヒドラジツド、トリヒドラゾトリアジ
ン、p−トルエンスルホニルセミカルバジツド、
又はN,N′−ジニトロソペンタメチレンテトラ
ミンである特許請求の範囲第1項ないし第3項い
ずれか記載の導電性樹脂組成物の製造方法。 5 化学発泡剤を、熱可塑性樹脂に対して2〜30
重量%の割合で配合する特許請求の範囲第1項な
いし第4項いずれか記載の導電性樹脂組成物の製
造方法。 6 収束剤を、導電性繊維に対して5〜40重量%
の割合で配合する特許請求の範囲第1項ないし第
5項いずれか記載の導電性樹脂組成物の製造方
法。 7 ペレツトの長さが、3〜12mmである特許請求
の範囲第1項ないし第6項いずれか記載の導電性
樹脂組成物の製造方法。
[Claims] 1. A sizing agent containing a thermoplastic resin and a chemical foaming agent is dissolved in a solvent, conductive fibers are immersed in the sizing agent and converged, dried to volatilize the solvent, and then cut into pellets. A method for producing a conductive resin composition, characterized by: 2. The conductive resin composition according to claim 1, wherein the conductive fibers are stainless steel fibers, aluminum fibers, copper fibers, carbon fibers, or carbon fibers having a metal plating layer on the surface, glass fibers, or organic fibers. Production method. 3 The number of conductive fibers coated and bundled with a binding agent is
The method for producing a conductive resin composition according to claim 1 or 2, wherein the number of conductive resin compositions is 500 to 20,000. 4 The chemical blowing agent is azodicarbonamide, azobisisobutyronitrile, 4,4'-oxybisbenzenesulfonylhydrazide, p-toluenesulfonylhydrazide, trihydrazotriazine, p-toluenesulfonyl semicarbazine. Do,
or N,N'-dinitrosopentamethylenetetramine, the method for producing a conductive resin composition according to any one of claims 1 to 3. 5 Add a chemical blowing agent to the thermoplastic resin at a ratio of 2 to 30%.
A method for producing a conductive resin composition according to any one of claims 1 to 4, wherein the conductive resin composition is blended in a proportion of % by weight. 6 5 to 40% by weight of sizing agent based on the conductive fibers
A method for producing a conductive resin composition according to any one of claims 1 to 5, wherein the conductive resin composition is blended in a proportion of . 7. The method for producing a conductive resin composition according to any one of claims 1 to 6, wherein the pellets have a length of 3 to 12 mm.
JP19517786A 1986-08-22 1986-08-22 Electrically conducting resin composition Granted JPS6351109A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19517786A JPS6351109A (en) 1986-08-22 1986-08-22 Electrically conducting resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19517786A JPS6351109A (en) 1986-08-22 1986-08-22 Electrically conducting resin composition

Publications (2)

Publication Number Publication Date
JPS6351109A JPS6351109A (en) 1988-03-04
JPH0414844B2 true JPH0414844B2 (en) 1992-03-16

Family

ID=16336726

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19517786A Granted JPS6351109A (en) 1986-08-22 1986-08-22 Electrically conducting resin composition

Country Status (1)

Country Link
JP (1) JPS6351109A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0649359A (en) * 1992-07-30 1994-02-22 Nippon G Ii Plast Kk Conductive resin composition
JP3073988B1 (en) 1999-08-12 2000-08-07 株式会社神戸製鋼所 Manufacturing method of organic fiber reinforced resin pellets

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50149747A (en) * 1974-05-22 1975-12-01
JPS53138466A (en) * 1977-05-09 1978-12-02 Ibm Pellets for thermoplastic molding
JPS56104012A (en) * 1980-01-22 1981-08-19 Teijin Chem Ltd Manufacture of stabilizer master pellet
JPS5922710A (en) * 1982-07-30 1984-02-06 Toshiba Chem Corp Manufacture of electroconductive molding material

Also Published As

Publication number Publication date
JPS6351109A (en) 1988-03-04

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