JPS6227445A - Production of electrically conductive resin composition - Google Patents

Production of electrically conductive resin composition

Info

Publication number
JPS6227445A
JPS6227445A JP16729985A JP16729985A JPS6227445A JP S6227445 A JPS6227445 A JP S6227445A JP 16729985 A JP16729985 A JP 16729985A JP 16729985 A JP16729985 A JP 16729985A JP S6227445 A JPS6227445 A JP S6227445A
Authority
JP
Japan
Prior art keywords
polyolefin
powder
solvent
mixture
conductive
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP16729985A
Other languages
Japanese (ja)
Inventor
Yoshio Matsumoto
良雄 松本
Toshio Fujii
敏雄 藤井
Fumiaki Takeuchi
竹内 史章
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 Kasei Corp
Original Assignee
Mitsubishi Kasei Corp
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 Kasei Corp filed Critical Mitsubishi Kasei Corp
Priority to JP16729985A priority Critical patent/JPS6227445A/en
Publication of JPS6227445A publication Critical patent/JPS6227445A/en
Pending legal-status Critical Current

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  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Conductive Materials (AREA)

Abstract

PURPOSE:To obtain a resin compsn. which has high electrical conductivity an little variation in electrical conductivity, by subjecting a slurry contg. and electrically conductive power and a polyolefin crystallized from a solvent to a solid/liquid separation treatment and reacting a radical generating agent with the resulting mixture. CONSTITUTION:A polyolefin and an electrically conductive powder are mixed with a polyolefin-dissolving solvent to dissolve the polyolefin in the solvent and to disperse uniformly the powder in the soln. The polyolefin is crystallized from said solvent contg. the polyolefin dissolved therein and the powder dispersed therein in the presence of a polyolefin-nondissolving poor solvent. A slurry contg. the crystallized polyolefin and the powder is subjected to a solid/ liquid separation treatment obtain a mixture of the polyolefin and the powder. A radical generating agent is added to the mixture. decomposed and reacted with the polyolefin to obtain the desired electrically conductive resin compsn.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリオレフィンと導電性粉末とから成る導電性
樹脂組成物の製造法に関するものである。詳しくは、高
い導電性を有し、且つ導電性のバラツキが小さく、しか
も強度特性に優れたポリオレフィンと導電性粉末とから
成る導電性樹脂組成物の製造法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing a conductive resin composition comprising a polyolefin and a conductive powder. Specifically, the present invention relates to a method for producing a conductive resin composition comprising a polyolefin and conductive powder that has high conductivity, small variations in conductivity, and excellent strength characteristics.

〔従来の技術〕[Conventional technology]

従来より、熱可塑性樹脂に種々の方法で導電性を付与さ
せた、いわゆる導電性樹脂は、成形加工の容易さなどの
熱可塑性樹脂の特徴を有しており、帯電防止用品、電気
機器用部品、導電性接着剤などの用途に広く使用されて
いる。該導電性樹脂を製造する方法としては、不導電体
である熱可塑性樹脂ioo重量部に対し、導電性粉体、
例えばカーボンブラックまたは黒鉛を!Q重置部前後添
加し、バンバリーミキサ−または熱ロールで、あるいは
それらの併用で、混練して成形する方法が知られている
Conventionally, so-called conductive resins, which are made by imparting conductivity to thermoplastic resins using various methods, have the characteristics of thermoplastic resins such as ease of molding, and are used as antistatic products and parts for electrical equipment. It is widely used in applications such as conductive adhesives. As a method for manufacturing the conductive resin, conductive powder,
For example carbon black or graphite! A method is known in which Q is added before and after the overlapping section and kneaded and molded using a Banbury mixer, a hot roll, or a combination thereof.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

しかしながら、上記方法で得られた該導電性樹脂は、電
気抵抗が高く、一般には体積抵抗率(ま九は体積固有抵
抗ともいう。)が703〜105Ω・G程度であり、ま
た該樹脂と導電性粉末との混合不均一により、同一製造
バッチでの体積抵抗率のバラツキが大きいという問題が
ある。
However, the conductive resin obtained by the above method has a high electrical resistance, and generally has a volume resistivity (also referred to as volume resistivity) of about 703 to 105 Ω・G, and is conductive with the resin. There is a problem in that the volume resistivity varies greatly in the same production batch due to non-uniform mixing with the bulk powder.

ま九、上記方法により体積抵抗率を102Ω・α以下に
するには、上記のカーボンブラック又は黒鉛をさらに多
量、すなわち50重量部以上添加する必要があシ、これ
により該樹脂と導電性粉末との混合がさらに不均一にな
り、上記抵抗値のバラツキがさらに大きくなるばかりで
なく、樹脂の特性、すなわち、成形性が低下し、実用的
に満足しうる導電性樹脂の成形物は得られない。
Ninth, in order to reduce the volume resistivity to 102Ω・α or less using the above method, it is necessary to add a larger amount of the above carbon black or graphite, that is, 50 parts by weight or more. The mixture becomes even more uneven, which not only increases the variation in the resistance value but also deteriorates the properties of the resin, that is, the moldability, making it impossible to obtain a molded product of conductive resin that is practically satisfactory. .

〔問題点を解決する次めの手段〕[Next method to solve the problem]

本発明者等はかかる従来技術に鑑み、高い導電性を有し
、且つ、導電性のバラツキが少々く、しかも強度特性に
優れた導電性樹脂組成物を製造すべく、鋭意検討を重ね
た結果、ポリオレフィン溶液に導電性粉末を添加し、次
いで晶出させて得た混合物にラジカル発生剤を添加反応
させることにより、高い導電性を有し、且つ導電性のバ
ラツキが少なく、しかも強度特性に優れた導電性樹脂組
成物が得られることを見出し、本発明を完成した。
In view of such prior art, the inventors of the present invention have conducted extensive studies in order to produce a conductive resin composition that has high conductivity, has little variation in conductivity, and has excellent strength characteristics. By adding a conductive powder to a polyolefin solution and then adding a radical generator to the resulting mixture, it has high conductivity, has little variation in conductivity, and has excellent strength properties. The inventors have discovered that a conductive resin composition can be obtained, and have completed the present invention.

すなわち、本発明の要旨は、ポリオレフィン可溶性溶媒
にポリオレフィン及び導電性粉末を添加して混合し、こ
れにポリオレフィン不溶性貧溶媒を添加してポリオレフ
ィンを晶出させ、晶出したポリオレフィンと導電性粉末
を含有するスラリーを固液分離し、得られたポリオレフ
ィン及び導電性粉末との混合物にラジカル発生剤を該ポ
リオレフイン1ooxx部に対して0.000 /〜j
重景重量加し、該ラジカルを分解して該ポリオレフィン
と反応させることを特徴とする導電性樹脂組成物の製造
法に存する。
That is, the gist of the present invention is to add and mix a polyolefin and a conductive powder to a polyolefin-soluble solvent, add a polyolefin-insoluble poor solvent to this to crystallize a polyolefin, and prepare a polyolefin containing the crystallized polyolefin and a conductive powder. The slurry is solid-liquid separated, and a radical generator is added to the mixture of the obtained polyolefin and conductive powder at a rate of 0.000/~j to 10xx parts of the polyolefin.
The present invention relates to a method for producing a conductive resin composition, characterized in that the radicals are decomposed and reacted with the polyolefin.

以下、本発明をさらに詳細に説明する。The present invention will be explained in more detail below.

本発明に用いられるポリオレフィンとしては、低密度ポ
リエチレン、中密度ポリエチレン、高密度ポリエチレン
、ポリブテン−/、ボリーダーメチルペンテンー/、エ
チレン−プロピレン共重合体、エチレン−ブテン−/共
重合体、エチレン−酢酸ビニル共重合体、エチレン−ア
ク重合体、及びこれらの混合物などが挙げられる。
The polyolefins used in the present invention include low density polyethylene, medium density polyethylene, high density polyethylene, polybutene/, boiler methylpentene/, ethylene-propylene copolymer, ethylene-butene/copolymer, ethylene- Examples include vinyl acetate copolymers, ethylene-ac polymers, and mixtures thereof.

lc、導電性粉末としては、導電性カーボンブラック、
黒鉛、金属粉末等の導電性粉末が挙げられ、特に導電性
カーボンブラックが好適にFurnace )、EI 
CF (5uper Conductive Furn
ace)。
lc, as the conductive powder, conductive carbon black,
Examples include conductive powders such as graphite and metal powders, with conductive carbon black being particularly preferred.
CF (5uper Conductive Furn)
ace).

OF (conauctive Furnace )、
チャンネル法のCG (CoroLuclve Cha
nnel )、アセチレンブラック等が挙げられる。
OF (conactive furnace),
Channel method CG (CoroLucle Cha)
nnel), acetylene black, etc.

さらに、上記ポリオレフィンを溶解させるのに用いられ
るポリオレフィン可溶性溶媒としては、ヘキサン、ヘプ
タン等の脂肪族炭化水素、ベンゼン、トルエン、キシレ
ン等の芳香族炭化レフ、トリクレン、モノクロルベンゼ
ン、ジクロルベンゼン等の塩素化炭化水素などが挙げら
れる。
Furthermore, the polyolefin-soluble solvent used to dissolve the above-mentioned polyolefin includes aliphatic hydrocarbons such as hexane and heptane, aromatic hydrocarbons such as benzene, toluene, and xylene, and chlorine such as trichlene, monochlorobenzene, and dichlorobenzene. Examples include hydrogenated hydrocarbons.

本発明においては、まず、上記ポリオレフィン可溶性溶
媒にポリオレフィン及び導電性粉末を添加、混合し、ポ
リオレフィンを該溶媒に溶解させると共に、導電性粉末
を溶液中に均一に分散させる。該溶媒中へのポリオレフ
ィンの添加時期については、特に制限がなく、導電性粉
末を添加する前に添加する方法、導電性粉末と同時に添
加する方法及び導電性粉末を添加後に添加する方法等い
ずれの方法で行ってもよい。
In the present invention, first, a polyolefin and a conductive powder are added to and mixed with the polyolefin-soluble solvent, the polyolefin is dissolved in the solvent, and the conductive powder is uniformly dispersed in the solution. There is no particular restriction on the timing of adding the polyolefin to the solvent, and it may be added before adding the conductive powder, added at the same time as the conductive powder, or added after the conductive powder, etc. You can also do it by method.

ポリオレフィンの添加量は、上記溶媒10θ重量部釦対
し、通常/重量部以上、好ましくは3〜4to重量部、
さらに好ましくは5〜36重量部の範凹である。該ポリ
オレフィンの添加量が7重量部未満では、上記溶媒の使
用量が多くなり、経済的でなく、まfcダO重量部より
多い場合には、ポリオレフィンを溶解させるのに時間大
する上、導電性粉末を該溶液中に均一に分散させるのが
困難となるので工業的ではない。また、ポリオレフィン
を上記溶媒に溶解させる温度は、通常常温以上、望まし
くは50℃以上その溶媒の沸点以下の温度で少なくとも
30分以上、望ましくは30〜/コO分間攪拌すること
により実施される。
The amount of polyolefin added is usually 3 to 4 parts by weight or more, preferably 3 to 4 parts by weight, per 10 parts by weight of the above solvent.
More preferably, the range is 5 to 36 parts by weight. If the amount of the polyolefin added is less than 7 parts by weight, the amount of the solvent used increases, which is not economical; if it is more than 7 parts by weight, it takes a long time to dissolve the polyolefin, and the conductivity is reduced. This method is not industrially practical because it is difficult to uniformly disperse the powder in the solution. The temperature at which the polyolefin is dissolved in the above-mentioned solvent is usually at least room temperature, preferably at least 50° C. and at most the boiling point of the solvent, and stirring is carried out for at least 30 minutes, preferably for 30 to 10 minutes.

上記導電性粉末の添加量は、所望とされるポリオレフィ
ンの体積抵抗率の範囲(109〜/θ−2Ω・σ)によ
り任意に選択されうるが、体積抵抗率を10Ω・α以下
とする場合には、ポリオレフイン10θ重量部に対し、
導電性粉末、例えば導電性カーボンブラックまたは黒鉛
が100重量部以上、望ましくは100〜300重量部
の範囲で用いられる。
The amount of the conductive powder added can be arbitrarily selected depending on the desired volume resistivity range of the polyolefin (109~/θ-2Ω・σ), but when the volume resistivity is set to 10Ω・α or less, is based on the weight of polyolefin 10θ,
A conductive powder such as conductive carbon black or graphite is used in an amount of 100 parts by weight or more, preferably in the range of 100 to 300 parts by weight.

本発明においては、上記のようにして得られた導電性粉
末が、均一に分散されたポリオレフィンを含有する混合
物をポリオレフィン不溶性貧溶媒の存在下でポリオレフ
ィンを晶出させ、晶出したポリオレフィンと導電性粉末
を含有するスラリーを固液分離してポリオレフィンと導
電性粉末との混合物を取得するものである。ポリオレフ
ィン不溶性貧溶媒としては、通常メチルアルコール、エ
チルアルコール、プロピルアルコール、メチルアルコー
ル等の炭素e/〜!個のアルコール類が用いられる。該
貧溶媒の使用量は(該貧溶媒)/(ポリオレフィン可溶
性溶媒)の重号比で通常772以上、好ましくは//2
〜コ0//、さらに好ましくVi///〜!//の範囲
で用いられる。上記混合物を該貧溶媒の存在下にポリオ
レフィンを晶出させる方法としては、該混合物中に該貧
溶媒を添加してポリオレフィンを晶出させる方法、ある
いは該貧溶媒中罠該混合物を添加してポリオレフィンを
晶出させる方法のいずれでもよい。上記ポリオレフィン
を晶出させる際の晶出温度としては、該貧溶媒の沸点以
下の温度、望ましくは!θ℃以下の温度で実施される。
In the present invention, the conductive powder obtained as described above is obtained by crystallizing the polyolefin from a mixture containing uniformly dispersed polyolefin in the presence of a polyolefin-insoluble poor solvent, and then combining the crystallized polyolefin and the conductive powder. A slurry containing powder is subjected to solid-liquid separation to obtain a mixture of polyolefin and conductive powder. Polyolefin-insoluble poor solvents are usually carbon e/~! such as methyl alcohol, ethyl alcohol, propyl alcohol, methyl alcohol, etc. Alcohols are used. The amount of the poor solvent used is usually 772 or more in terms of the weight ratio of (the poor solvent)/(polyolefin-soluble solvent), preferably //2.
~Co0//, more preferably Vi///~! Used in the range //. The method of crystallizing the polyolefin from the above mixture in the presence of the poor solvent includes a method of adding the poor solvent to the mixture to crystallize the polyolefin, or a method of adding the mixture to the poor solvent to crystallize the polyolefin. Any method of crystallizing may be used. The crystallization temperature when crystallizing the polyolefin is preferably a temperature below the boiling point of the poor solvent! It is carried out at a temperature below θ°C.

上記のようKして晶出したポリオレフィンと導電性粉末
とを含有するスラリーは、必要に応じて静置したのち、
通常の固液分離法、例えば濾過、遠心分離等により、固
液分離して、ポリオレフィンと導電性粉末との混合物を
得る。得られたポリオレフィンと導電性粉末との混合物
は、必要に応じて該貧溶媒で洗浄し九のち、乾燥処理さ
れる。
The slurry containing the polyolefin and conductive powder crystallized by K as described above is left to stand as necessary, and then
A mixture of polyolefin and conductive powder is obtained by performing solid-liquid separation using a conventional solid-liquid separation method such as filtration or centrifugation. The obtained mixture of polyolefin and conductive powder is washed with the poor solvent if necessary, and then dried.

本発明の導電性樹脂組成物は、上記したポリオレフィン
と導電性粉末との混合物に、さらにラジカル発生剤を添
加して、ラジカル発生剤を分解させ、該ポリオレフィン
と反応せしめたものである。
The conductive resin composition of the present invention is obtained by further adding a radical generator to the above-described mixture of polyolefin and conductive powder, decomposing the radical generator, and reacting with the polyolefin.

上記したポリオレフィンと導電性粉末との混合物に添加
するラジカル発生剤としては、半減期7分となる分解温
度が730℃〜3θθ℃の範囲のものが好ましく、例え
ばジクミルパーオキサイド、コ、!−ジメチルーコ、!
−ジ(t−ブチルパーオキシ)ヘキサン、−1!−ジメ
チル−2、j−ジ(1−ブチルパーオキシ)ヘキシン−
3、α、α′−ビス(1−プチルバーオキシイソグロビ
ル)ベンゼン、ジベンゾイルパーオキサイド、ジ−t−
ブチルパーオキサイド等が挙げられる。
The radical generator to be added to the above-mentioned mixture of polyolefin and conductive powder is preferably one with a decomposition temperature in the range of 730°C to 3θθ°C with a half-life of 7 minutes, such as dicumyl peroxide, co-! -Dimethylco,!
-di(t-butylperoxy)hexane, -1! -dimethyl-2,j-di(1-butylperoxy)hexyne-
3, α, α′-bis(1-butylbaroxyisoglobil)benzene, dibenzoyl peroxide, di-t-
Examples include butyl peroxide.

ラジカル発生剤の添加量は、上記ポリオレフィン100
重量部に対し、0.000 /〜j重量部、好ましくは
0,00.2〜−21i量部の範囲内から選ばれるが、
この添加量がO0θOθ/it部よシ少ない場合には、
本発明の効果が顕著に表われず、例えば、成形品とした
場合の強度特性が無添加のものと殆んど変らず、また、
5重量部より多い場合には、添加したラジカル発生剤の
分散性が悪く、均一に分散する前にポリオレフィンと局
部的に反応を生起し、得られる該組成物の強度特性及び
体積抵抗率のバラツキが大きくなるので好ましくない。
The amount of radical generator added is 100% of the above polyolefin.
selected from the range of 0.000/~j parts by weight, preferably 0.00.2~-21i parts by weight,
If this addition amount is less than O0θOθ/it part,
The effects of the present invention are not noticeable, for example, the strength properties of molded products are almost the same as those without additives, and
If the amount is more than 5 parts by weight, the added radical generator will have poor dispersibility and will locally react with the polyolefin before being uniformly dispersed, resulting in variations in the strength properties and volume resistivity of the resulting composition. This is not preferable because it increases the size.

本発明において、上記ポリオレフィンと導電性粉末との
混合物にラジカル発生剤を添加して、ラジカル発生剤を
分解させ、該ポリオレフィンと反応せしめる方法として
は、特に制限を設けるものではなく、例えば以下の方法
で実施することかできる。
In the present invention, the method of adding a radical generator to the mixture of the polyolefin and conductive powder, decomposing the radical generator, and reacting with the polyolefin is not particularly limited, and for example, the following method is used. It can be carried out with

(1)押出機、バンバリーミキサ−等の混抄機を使用し
て、上記ポリオレフィンと導電性粉末との混合物、及び
ラジカル発生剤を混練した後、ペレット化し、該ベレッ
トを使用してプレス成形または圧縮成形を行なう際該ラ
ジカル発生剤とポリオレフィンを反応させる。
(1) Using a mixing machine such as an extruder or a Banbury mixer, the mixture of the polyolefin and conductive powder and the radical generator are kneaded, pelletized, and then press-molded or compressed using the pellets. During molding, the radical generator and polyolefin are reacted.

(2)成形時、例えばプレス成形または圧縮成形時に、
上記ポリオレフィンと導電性粉末との混合物及びラジカ
ル発生剤を同時に、fたは順次にフィードして溶融成形
する際、ラジカル発生剤とポリオレフィンを反応させる
(2) During molding, for example press molding or compression molding,
When the mixture of the polyolefin and conductive powder and the radical generator are fed simultaneously or sequentially and melt-molded, the radical generator and the polyolefin are reacted.

(3)  ラジカル発生剤を多量に含んだマスターバッ
チ(ポリオレフィンに多量のラジカル発生剤を該ポリオ
レフィンの融点以上の温度で、且つ該ポリオレフィンと
ラジカル発生剤との反応が極めて遅い温度下、例えば7
30〜760℃の温度下で溶融混練した高濃度(通常2
00 ppm −20%程度)のラジカル発生剤を含有
するポリオレフィンのマスターバッチ)をあらかじめ作
シ、このiスターバッチと上記ポリオレフィンと導電性
粉末との混合物をブレンドし、プレス成形または圧縮成
形を行なう。
(3) A masterbatch containing a large amount of a radical generator (a large amount of a radical generator is added to a polyolefin at a temperature higher than the melting point of the polyolefin and at a temperature at which the reaction between the polyolefin and the radical generator is extremely slow, e.g.
High concentration (usually 2
A polyolefin masterbatch containing a radical generating agent of about 0.00 ppm -20% is prepared in advance, and this i-starbatch is blended with a mixture of the polyolefin and conductive powder, followed by press molding or compression molding.

ま次、上記(2)または(3)の方法で、ポリオレフィ
ンとラジカル発生剤との反応を十分に行なわせずに成形
し、該成形品を成形温度以上の温度で熱処理して、反応
を完結させる方法で行なってもよい。
Next, by the method (2) or (3) above, the polyolefin and the radical generator are molded without sufficiently reacting, and the molded product is heat-treated at a temperature higher than the molding temperature to complete the reaction. It may also be done in the following manner.

また、ラジカル発生剤そのものはそのまま、或いは溶剤
に溶かして使用される。
Further, the radical generator itself may be used as it is or dissolved in a solvent.

上記ポリオレフィンと導電性粉末との混合物をラジカル
発生剤と反応させることによシ、該ポリオレフィンが架
橋反応を生起して分子間でのクロスリングが起り、分子
間力が増加し、一部がゲル化状態となり、シート等の成
形品とした場合の衝!1強度及び引張強度等の強度特性
が著しく向上された導電性樹脂組成物が得られる。
By reacting the mixture of the above-mentioned polyolefin and conductive powder with a radical generator, the polyolefin undergoes a cross-linking reaction, cross-ring occurs between molecules, the intermolecular force increases, and a part of the polyolefin becomes gelatinous. When the product is made into a molded product such as a sheet, the impact occurs! A conductive resin composition with significantly improved strength properties such as 1 strength and tensile strength can be obtained.

また、本発明の導電性樹脂組成物にはその使用目的に応
じて抗酸化剤、紫外線吸収剤、熱安定剤、帯電防止剤、
顔料等の添加剤を適宜配合することができる。
The conductive resin composition of the present invention may also include antioxidants, ultraviolet absorbers, heat stabilizers, antistatic agents, etc. depending on the purpose of use.
Additives such as pigments can be added as appropriate.

〔実施例〕〔Example〕

実施例/ (a)  ポリオレフィンとカーボンブラックとの混合
物の製造 容量’llのフラスコにバラキシレン/610rnlc
/%009)及び導電性カーボンブラック(平均粒径♂
0μ)302を装入し、攪拌しながら、液温を7.20
′Cまで昇温し、これに高圧法低密度ポリエチレン(密
度:0.り/L!″y /cnI 、メルトインデック
ス:10f/10分)70?添加して攪拌しながら、7
20℃で7時間保持したのち、7j’Cjで冷却し、こ
れにエチルアルコール2tを添加し、23℃の温度で3
0分間保持してポリオレフィンをカーボンブラック表面
上に晶出させた。晶出したポリオレフィンとカーボンブ
ラックとを含有するスラリーを23℃で濾過して固液分
離し、得られたポリオレフィンとカーボンブラックとの
混合物をエチルアルコール/lで洗浄し念のち、−昼夜
放置して風乾し、さらに70〜7j℃の温度で70時間
真空乾燥して、ポリオレフィンとカーボンブラックとの
混合物粉末999を得た。
Examples / (a) Production of a mixture of polyolefin and carbon black
/%009) and conductive carbon black (average particle size ♂
0μ) 302, and while stirring, lower the liquid temperature to 7.20.
The temperature was raised to 'C, and to this was added high-pressure low density polyethylene (density: 0.li/L!"y/cnI, melt index: 10f/10 minutes) 70? with stirring.
After holding at 20°C for 7 hours, it was cooled at 7j'Cj, 2t of ethyl alcohol was added thereto, and the mixture was heated at 23°C for 3 hours.
The polyolefin was held for 0 minutes to crystallize on the carbon black surface. The slurry containing the crystallized polyolefin and carbon black was filtered at 23°C for solid-liquid separation, and the resulting mixture of polyolefin and carbon black was washed with ethyl alcohol/l, and then left to stand day and night. It was air-dried and further vacuum-dried at a temperature of 70 to 7JC for 70 hours to obtain a polyolefin and carbon black mixture powder 999.

(b)  導電性樹脂組成物の製造及びその評価上官i
i’ (a)で得られたポリオレフィン及びカーボンブ
ラックの混合物粉末100重景重量ジクミルパーオキサ
イド7.0重量部をロール混合し、これを730℃の温
度でプレス成形して厚さ/wRのシート状にした。得ら
れたシートを760℃の温度で20分間以上熱処理し、
未反応のラジカル発生剤とポリオレフィンとの反応を完
結せしめ念。該シートにつき衝撃強度、引張強度、体積
抵抗率及び体積抵抗率のバラツキを下記方法で測定した
(b) Manufacture and evaluation of conductive resin compositions i
i' 7.0 parts by weight of dicumyl peroxide (100 gm) of the polyolefin and carbon black mixture powder obtained in (a) was mixed in a roll, and this was press-molded at a temperature of 730°C to a thickness/wR. Made into a sheet. The obtained sheet is heat treated at a temperature of 760°C for 20 minutes or more,
It is important to complete the reaction between the unreacted radical generator and the polyolefin. The impact strength, tensile strength, volume resistivity, and variation in volume resistivity of the sheet were measured using the following methods.

なお、体積抵抗率は温度20℃、湿度6!チの恒温下に
体積抵抗率測定用電極(安藤電■製、デジタルマルチメ
ーターJ%&jB型)により測定した。
In addition, the volume resistivity is at a temperature of 20°C and a humidity of 6! The volume resistivity was measured using an electrode for measuring volume resistivity (manufactured by Ando Denki, digital multimeter J% & jB type) under constant temperature conditions.

衝撃強度はASTM D //、!、2 K準じて行っ
た。
Impact strength is ASTM D //,! , 2K.

引張強度はJ工SK乙7乙θに準じて行った。The tensile strength was determined according to J-Kotsu SK Otsu 7 Otsu θ.

結果を表/に示す。The results are shown in Table/.

実施例コ 実施例/において、導電性カーボンブラックと高圧法低
密度ポリエチレンの混合割合を表/のように変えたこと
以外は、実施例/と同様にして行つ九。その結果を表/
に示す。
Example 9 The same procedure as in Example 9 was carried out except that the mixing ratio of conductive carbon black and high-pressure low density polyethylene was changed as shown in Table 9. Show the results/
Shown below.

比較例/ 実施例/で用いたのと同じ原料を用い、高圧法低密度ポ
リエチレン70′N量部に導電性カーボンブラック30
重量部を添加したものを、ロール混練機を用いて7.2
0℃の温度で30分間混練して、導電性樹脂組成物を製
造したこと以外は、実施例/(b)と同様にして行った
。その結果を表/に示す。
Using the same raw materials as those used in Comparative Example/Example/, 30 parts of conductive carbon black was added to 70'N parts of high-pressure low-density polyethylene.
7.2 parts by weight was added using a roll kneader.
The process was carried out in the same manner as in Example/(b), except that the conductive resin composition was manufactured by kneading at a temperature of 0° C. for 30 minutes. The results are shown in Table/.

比較例コ 比較例/において、高圧法低密度ポリエチレン導電性カ
ーボンブラックの混合割合を表/のように変えたこと以
外は、比較例/と同様にして行った。結果を表/に示す
Comparative Example Comparative Example 1 was carried out in the same manner as Comparative Example 1, except that the mixing ratio of high-pressure low density polyethylene conductive carbon black was changed as shown in Table 1. The results are shown in Table/.

〔発明の効果〕〔Effect of the invention〕

本発明によって得られる導電性樹脂組成物は従来の方法
で得られるものに比べ、高い導電性を有し、且つ導電性
のバラツキが小さく、しかも強度特性に優れたものが得
られる。従って、本発明方法で得られ良導電性樹脂組成
物は電池の電極、抵抗体、帯電防止材料、高圧ケーブル
、導電性基板、発熱体素子、電界遮蔽材料、破覆材等に
好適に利用することができる。特に抵抗体に用いた場合
には導電体が均一に分散されているため均一に電流が流
れ、従来品で見受けられた電流の暴走がないので、回路
の破壊が防止できるので好ましい。
The conductive resin composition obtained by the present invention has higher conductivity than those obtained by conventional methods, has less variation in conductivity, and has excellent strength properties. Therefore, the highly conductive resin composition obtained by the method of the present invention is suitably used for battery electrodes, resistors, antistatic materials, high-voltage cables, conductive substrates, heating elements, electric field shielding materials, breaking materials, etc. be able to. Particularly when used in a resistor, since the conductor is uniformly distributed, the current flows uniformly, and there is no current runaway that is observed in conventional products, which prevents damage to the circuit, which is preferable.

出 願 人  三菱化成工業株式会社 代 理 人  弁理士 長谷用   −ほか/名Sender: Mitsubishi Chemical Industries, Ltd. Representative Patent Attorney Hase - Others/Names

Claims (1)

【特許請求の範囲】[Claims] (1)ポリオレフィン可溶性溶媒にポリオレフィン及び
導電性粉末を添加して混合し、これにポリオレフィン不
溶性貧溶媒を添加してポリオレフィンを晶出させ、晶出
したポリオレフィンと導電性粉末を含有するスラリーを
固液分離し、得られたポリオレフィン及び導電性粉末の
混合物にラジカル発生剤を該ポリオレフィン100重量
部に対して0.0001〜5重量部添加し、該ラジカル
発生剤を分解して該ポリオレフィンと反応させることを
特徴とする導電性樹脂組成物の製造法
(1) Polyolefin and conductive powder are added to a polyolefin-soluble solvent and mixed, a polyolefin-insoluble poor solvent is added to this to crystallize the polyolefin, and a slurry containing the crystallized polyolefin and conductive powder is converted into a solid liquid. Separating, adding 0.0001 to 5 parts by weight of a radical generator to 100 parts by weight of the polyolefin to the obtained mixture of the polyolefin and conductive powder, decomposing the radical generator and reacting with the polyolefin. A method for producing a conductive resin composition characterized by
JP16729985A 1985-07-29 1985-07-29 Production of electrically conductive resin composition Pending JPS6227445A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16729985A JPS6227445A (en) 1985-07-29 1985-07-29 Production of electrically conductive resin composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16729985A JPS6227445A (en) 1985-07-29 1985-07-29 Production of electrically conductive resin composition

Publications (1)

Publication Number Publication Date
JPS6227445A true JPS6227445A (en) 1987-02-05

Family

ID=15847176

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16729985A Pending JPS6227445A (en) 1985-07-29 1985-07-29 Production of electrically conductive resin composition

Country Status (1)

Country Link
JP (1) JPS6227445A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009230951A (en) * 2008-03-21 2009-10-08 Nec Corp Polymer radical material-conductive material complex, method of manufacturing the same, and energy storage device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009230951A (en) * 2008-03-21 2009-10-08 Nec Corp Polymer radical material-conductive material complex, method of manufacturing the same, and energy storage device

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