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JPH11172146A - Conductive carbon black - Google Patents

Conductive carbon black

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Publication number
JPH11172146A
JPH11172146A JP34498997A JP34498997A JPH11172146A JP H11172146 A JPH11172146 A JP H11172146A JP 34498997 A JP34498997 A JP 34498997A JP 34498997 A JP34498997 A JP 34498997A JP H11172146 A JPH11172146 A JP H11172146A
Authority
JP
Japan
Prior art keywords
carbon black
heat treatment
total oxygen
oxygen content
resin
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
JP34498997A
Other languages
Japanese (ja)
Inventor
Hideyuki Hisa
英之 久
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 Chemical Corp
Original Assignee
Mitsubishi Chemical 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 Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP34498997A priority Critical patent/JPH11172146A/en
Publication of JPH11172146A publication Critical patent/JPH11172146A/en
Pending legal-status Critical Current

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  • Compositions Of Macromolecular Compounds (AREA)
  • Pigments, Carbon Blacks, Or Wood Stains (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain the subject carbon black capable of inparting a high electroconductivity to a resin when the carbon black is kneaded with the resin while keeping the sufficient processability and useful fur a hose for a solvent such as gasoline by carrying out a heat treatment of a specific furnace black in an inert gas atmosphere. SOLUTION: This carbon black is obtained by carrying out a heat treatment of a furnace black having <=20 mg/g total oxygen content before the heat treatment in an inert gas atmosphere so as to reduce 5-50%, preferably 5-30% of the total oxygen content. For example, the heat treatment is carried out in the presence of argon or the like at 200-700 deg.C for about 15 min-10 hr, and the carbon black having about 30 500 m<2> /g specific surface area, about 40-360 mL/100g DBP absorption and about 0.01-0.5% ash content is preferably used as the carbon black.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、導電性カーボンブ
ラックに関するものである。本発明導電性カーボンブラ
ックは、導電性に優れるので、各種用途に使用可能であ
る。具体的用途としては、ガソリン等溶剤用ホース、各
種コネクター、ドアハンドル部品等が挙げられ、特にこ
れらの用途向けに、樹脂に混合して、加工性を失わずに
導電性を付与するのに好適に用いられる。
The present invention relates to a conductive carbon black. Since the conductive carbon black of the present invention has excellent conductivity, it can be used for various applications. Specific applications include hoses for solvents such as gasoline, various connectors, door handle parts, etc., especially for these applications, suitable for imparting conductivity without loss of processability by mixing with resin. Used for

【0002】[0002]

【従来の技術】ポリカーボネート、ポリエチレンテレフ
タレート、ナイロン等の樹脂は、一般的には絶縁性であ
るが、用途によっては、導電性を要求されることがあ
る。これらの絶縁性の樹脂に導電性を付与するには、一
般的には導電性カーボンブラックを配合することが多用
されている。すなわち、このようなカーボンブラックと
しては、主としてアセチレンブラック、ケッチェンブラ
ック等が用いられており、金属と比べて軽量で、かつ安
価である等の利点を有する。
2. Description of the Related Art Resins such as polycarbonate, polyethylene terephthalate, and nylon are generally insulative, but may be required to have conductivity depending on applications. In order to impart conductivity to these insulating resins, generally, conductive carbon black is frequently used. That is, acetylene black, Ketjen black, or the like is mainly used as such carbon black, and has advantages such as light weight and low cost as compared with metal.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、これら
のカーボンブラックを配合した系では、例えば、ポリア
ミド樹脂等にカーボンブラックを配合した場合、導電性
を向上させるためにカーボンブラックの配合量を増やす
と、溶融粘度が高くなり射出成形等での成形加工が困難
となるだけでなく、成形できたとしても衝撃強度等の機
械的性質が劣った成型品しか得られない。
However, in a system in which these carbon blacks are blended, for example, when carbon black is blended in a polyamide resin or the like, if the blending amount of carbon black is increased to improve conductivity, Not only does the melt viscosity increase, making molding by injection molding or the like difficult, but even if molding is possible, only molded products with poor mechanical properties such as impact strength can be obtained.

【0004】より一般的には、高い導電性を得ようと多
量に配合すると、 1)粘度が高くなりすぎ、加工性が著しく低下する。 2)カーボンブラックの強い表面活性のため、架橋剤が
効果的に作用しない。 3)より高い導電性を得ようとしても、カーボンブラッ
クの配合量に物理的上限があり、得られる体積抵抗率に
制限があるといった難点が現れる場合がある。
[0004] More generally, when a large amount is blended in order to obtain high conductivity, 1) the viscosity becomes too high and the workability is remarkably reduced. 2) Due to the strong surface activity of carbon black, the crosslinking agent does not work effectively. 3) Even if an attempt is made to obtain higher conductivity, there may be a case where there is a physical upper limit in the compounding amount of carbon black and the obtained volume resistivity is limited.

【0005】[0005]

【課題を解決するための手段】本発明者らは、上記の課
題を解決すべく鋭意検討した結果、加熱処理前の全酸素
量が一定量以下であるファーネスブラックを、不活性雰
囲気下で加熱処理することにより全酸素量を5〜50%
低減してなるカーボンブラックが、樹脂に混練した場合
に十分な加工性を保持しながら高い導電性を付与し得る
ことを見出し、本発明に到達した。即ち、本発明は、加
熱処理前の全酸素量が20mg/g以下であるファーネ
スブラックを、不活性雰囲気下で加熱処理することによ
り、全酸素量を5〜50%低減してなることを特徴とす
る導電性カーボンブラックに存する。
Means for Solving the Problems The inventors of the present invention have conducted intensive studies to solve the above-mentioned problems, and have found that furnace black having a total oxygen content of not more than a predetermined amount before heat treatment is heated in an inert atmosphere. 5-50% of total oxygen content by processing
The present inventors have found that reduced carbon black can impart high conductivity while maintaining sufficient workability when kneaded with a resin, and have reached the present invention. That is, the present invention is characterized in that furnace black having a total oxygen content of 20 mg / g or less before heat treatment is subjected to heat treatment in an inert atmosphere to reduce the total oxygen content by 5 to 50%. Conductive carbon black.

【0006】[0006]

【発明の実施の形態】以下、本発明をより詳細に説明す
る。本発明導電性カーボンブラックは、加熱処理前の全
酸素量が20mg/g以下であるファーネスブラック
を、不活性雰囲気下で加熱処理することにより全酸素量
を5〜50%、好ましくは5〜30%低減してなるカー
ボンブラックである。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in more detail. The conductive carbon black of the present invention has a total oxygen content of 5 to 50%, preferably 5 to 30%, obtained by subjecting furnace black having a total oxygen content of 20 mg / g or less before heat treatment to heat treatment in an inert atmosphere. % Carbon black.

【0007】ここで、不活性雰囲気とは、酸素分子の存
在しない、或いは存在しても極めて構成比の低い雰囲気
をいい、具体的には、アルゴン、窒素、二酸化炭素など
で構成される雰囲気を指す。また、加熱処理温度として
は、200℃以上700℃以下が好ましい。200℃以
下では、酸素官能基が脱離しにくく、また700℃以上
になるとカーボンブラック粒子表面並びにアグリゲート
やアグロメートに焼き締まり現象が発生し、結果的に凝
集ユニットが固くなり、樹脂への分散性が悪くなること
がある。加熱処理時間は、温度にもよるが、15分〜1
0時間程度が好ましい。
Here, the inert atmosphere refers to an atmosphere in which oxygen molecules do not exist or have an extremely low composition ratio even when oxygen molecules exist. Specifically, an atmosphere composed of argon, nitrogen, carbon dioxide or the like is used. Point. Further, the heat treatment temperature is preferably from 200 ° C. to 700 ° C. At 200 ° C. or lower, oxygen functional groups are not easily desorbed, and at 700 ° C. or higher, a burning phenomenon occurs on the surface of carbon black particles and aggregates and agglomerates. May worsen. The heat treatment time depends on the temperature, but 15 minutes to 1 hour.
About 0 hours is preferable.

【0008】本発明に用いるカーボンブラックは、19
95年度カーボンブラック協会発行の「カーボンブラッ
ク便覧(第3版)」の3頁に記載されているオイルファ
ーネス法で得られるカーボンブラックの内、全酸素量が
20mg/g以下のカーボンブラックである。比表面積
は約30〜500m2/g、DBP吸収量は約40〜3
60ml/100g、灰分は約0.01〜0.5%が好
ましい。これらの物性値は、加熱処理前後であまり変動
がない。
The carbon black used in the present invention is 19
Among the carbon blacks obtained by the oil furnace method described on page 3 of "Carbon Black Handbook (Third Edition)" issued by the Carbon Black Association of 1995, those having a total oxygen content of 20 mg / g or less. The specific surface area is about 30 to 500 m 2 / g, and the DBP absorption is about 40 to 3
60 ml / 100 g, and the ash content is preferably about 0.01 to 0.5%. These physical property values do not change much before and after the heat treatment.

【0009】通常、カーボンブラックの粒子表面には、
水酸基やカルボニル基の酸素官能基が存在し、これの量
により、樹脂等に配合した際の抵抗が大幅に変化する。
酸素官能基は、揮発分組成で測定し、水酸基やカルボニ
ル基の量はCO、またカルボキシル基の量は、CO2
して定量でき、全酸素量はCOおよびCO2から換算し
た量である。
Usually, on the surface of the carbon black particles,
There is an oxygen functional group such as a hydroxyl group or a carbonyl group, and the amount thereof greatly changes the resistance when blended in a resin or the like.
The oxygen functional group is measured by volatile composition, the amount of hydroxyl group and carbonyl group can be quantified as CO, the amount of carboxyl group can be quantified as CO 2 , and the total oxygen amount is an amount converted from CO and CO 2 .

【0010】上記揮発分組成は、一定量の乾燥したカー
ボンブラックを耐熱性の試験管に入れ、10-2mmHg
以下までの減圧とした後、1500℃に加熱した電気炉
に装置し、30分間脱離する。これを全量タンクに集
め、混合した後、ガスクロマトグラフィーによってガス
の組成及び量を測定し、この結果から全酸素量を算出す
る。
[0010] The above volatile composition is determined by adding a fixed amount of dried carbon black to a heat-resistant test tube and placing it in a 10 -2 mmHg
After reducing the pressure to the following, the device is placed in an electric furnace heated to 1500 ° C. and desorbed for 30 minutes. After collecting and mixing the total amount in a tank, the composition and amount of the gas are measured by gas chromatography, and the total oxygen amount is calculated from the results.

【0011】本発明カーボンブラックは、樹脂に混練し
て導電性組成物として用いるのに適するが、その混練法
は、特に限定されるものではなく、ヘンシェルミキサー
等でドライブレンドした物を公知の単軸や2軸混練機で
連続的に混練してペレット化する方法が採用できる。樹
脂組成物とする際には、樹脂および本発明カーボンブラ
ック以外に、補強性充填剤、耐熱性向上剤、難燃剤、発
泡剤等の各種添加剤を随時付加的に配合してもよい。こ
のようなものとしては、通常、煙霧質シリカ、沈殿法シ
リカ、けいそう土等の補強性充填剤、酸化アルミニウ
ム、マイカ、クレイ、炭酸亜鉛、ガラスビーズ、ポリジ
メチルシロキサン、アルケニル基含有ポリシロキサン、
ポリシルセスキオキサン等が例示される。
The carbon black of the present invention is suitable for being kneaded with a resin to be used as a conductive composition, but the kneading method is not particularly limited, and a material obtained by dry blending with a Henschel mixer or the like is used. A method of continuously kneading with a shaft or a twin-screw kneader to form pellets can be employed. In preparing the resin composition, various additives such as a reinforcing filler, a heat resistance improver, a flame retardant, and a foaming agent may be optionally added in addition to the resin and the carbon black of the present invention. As such materials, usually, fumed silica, precipitated silica, reinforcing fillers such as diatomaceous earth, aluminum oxide, mica, clay, zinc carbonate, glass beads, polydimethylsiloxane, alkenyl group-containing polysiloxane,
Examples thereof include polysilsesquioxane.

【0012】[0012]

【実施例】以下、実施例によって本発明を更に詳細に説
明するが、本発明はその要旨を超えない限り、下記実施
例により限定されるものではない。 (実施例1)比表面積28m2/g、DBP吸収量13
0ml/100g、灰分0.06%で表1に示す揮発分
組成を有するファーネス法カーボンブラック500g
を、直径30cm、長さ50cmの円筒状SUS製キル
ンに入れ、10rpmで回転させた。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the scope of the invention. (Example 1) Specific surface area 28 m 2 / g, DBP absorption 13
500 g of furnace method carbon black having a volatile content shown in Table 1 with 0 ml / 100 g and ash content of 0.06%
Was placed in a cylindrical SUS kiln having a diameter of 30 cm and a length of 50 cm, and rotated at 10 rpm.

【0013】不活性雰囲気は、CO2ガスを用いた。C
2ガスは、キルンの中心部より10リットル/分の量
を挿入し、キルン内全域が完全に、CO2で置換された
後加熱を開始した。加熱はキルン全体を覆った電気炉を
用いカーボンブラックの温度が350℃±5℃になるよ
うにコントロールしつつ、60分間処理した。
As an inert atmosphere, CO 2 gas was used. C
O 2 gas was inserted at a rate of 10 liters / minute from the center of the kiln, and heating was started after the entire area of the kiln was completely replaced with CO 2 . Heating was performed for 60 minutes using an electric furnace covering the entire kiln while controlling the temperature of the carbon black to be 350 ° C. ± 5 ° C.

【0014】得られたカーボンブラックの物性は表1に
示した。このカーボンブラックを用いて、以下の通り、
導電性ナイロン樹脂組成物からなる成型物を製造した。
三菱エンジニアリングプラスチックス社製のナイロン6
樹脂、商品名「ノバミッド1020」73%、実施例1
で製造されたカーボンブラック22%、さらに東レ社製
N−n−ブチルベンゼンスルホナミド、商品名「BBS
A」5%を配合し、ヘンシェルミキサー(1000rp
m)で10分間混合した。
The physical properties of the obtained carbon black are shown in Table 1. Using this carbon black,
A molded article made of the conductive nylon resin composition was manufactured.
Nylon 6 manufactured by Mitsubishi Engineering-Plastics Corporation
Resin, product name “Novamid 1020” 73%, Example 1
22% carbon black manufactured by Toray Industries, Inc., and N-n-butylbenzenesulfonamide manufactured by Toray Co., Ltd., trade name “BBS
A "5%, and mixed with a Henschel mixer (1000 rpm)
m) for 10 minutes.

【0015】得られた混合物をスクリュー径35mmφ
の東芝機械社製商品名「TEM35」を用い、混練部の
温度275℃、樹脂温度270℃、フィード4kg/H
の条件で混練し、得たストランドを水冷後ペレタイザー
で切断し、ペレットを製造した。ペレットは、真空乾燥
機で70℃×12HR乾燥後、日本製鋼社製射出成型
機、商品名「J75ED」を用いて、シリンダー温度2
80℃、金型温度80℃、スクリュー回転数120rp
m、射出圧1039kg/m2の条件により射出成形し
た。射出成形に特に問題はなく、所望の形状で十分な導
電性を有する成形物を容易に得ることができた。 (実施例2)比表面積133m2/g、DBP吸収量1
16ml/100g、灰分0.03%で表1に示す揮発
分組成を有するファーネス法カーボンブラックを実施例
1と全く同様に加熱処理したカーボンブラックの物性を
表1に示す。得られたカーボンブラックを用いて、実施
例1と全く同様にして導電性ナイロン樹脂組成物からな
る成形物を製造したところ、射出成形に特に問題はな
く、所望の形状で十分な導電性を有する成形物を容易に
得ることができた。 (比較例1)実施例1で加熱処理に供したファーネス法
カーボンブラックを、加熱処理せずにそのまま用いて、
実施例1と全く同様にして導電性ナイロン樹脂組成物か
らなる成形物を製造したところ、成形時に樹脂組成物の
粘度が高すぎ、所望の形状に成形できなかった。また、
成型物の体積抵抗率も実施例と比較して大きかった。 (比較例2)加熱処理の際、CO2ガスのかわりに空気
を10リットル/分装入した以外、実施例1と全く同様
にして得たカーボンブラックの物性を表1に示す。得ら
れたカーボンブラックを用いて、実施例1と全く同様に
して導電性ナイロン樹脂組成物からなる成形物を製造し
たところ、成形時に樹脂組成物の粘度が高すぎ、所望の
形状に成形できなかった。また、成型物の体積抵抗率も
実施例と比較して著しく大きかった。 (比較例3)加熱処理を800℃で1時間行なった以
外、実施例1と全く同様にして得たカーボンブラックの
物性を表1に示す。得られたカーボンブラックを用い
て、実施例1と全く同様にして導電性ナイロン樹脂組成
物からなる成形物を製造したところ、成型物の体積抵抗
率は実施例と比較して大きかった。 (比較例4)比表面積225m2/g、DBP吸収量1
61ml/100g、灰分0.65%で表1に示す揮発
分組成を有するファーネス法カーボンブラックを実施例
1と全く同様に加熱処理したカーボンブラックの物性を
表1に示す。得られたカーボンブラックを用いて、実施
例1と全く同様にして導電性ナイロン樹脂組成物からな
る成形物を製造したところ、成型物の体積抵抗率は実施
例と比較して著しく大きかった。
[0015] The resulting mixture was screwed to a diameter of 35 mmφ.
Kneading part temperature 275 ° C, resin temperature 270 ° C, feed 4 kg / H
The resulting strand was water-cooled and cut with a pelletizer to produce a pellet. After the pellets were dried at 70 ° C. × 12 HR in a vacuum dryer, the cylinder temperature was adjusted to 2 using an injection molding machine (trade name “J75ED” manufactured by Nippon Steel Corporation).
80 ° C, Mold temperature 80 ° C, Screw rotation speed 120rpm
m and injection pressure of 1039 kg / m 2 . There was no particular problem in injection molding, and a molded article having a desired shape and sufficient conductivity could be easily obtained. (Example 2) Specific surface area 133 m 2 / g, DBP absorption 1
Table 1 shows the physical properties of the carbon black obtained by subjecting a furnace-process carbon black having a volatile composition shown in Table 1 to a heat treatment of 16 ml / 100 g and an ash content of 0.03% in exactly the same manner as in Example 1. Using the obtained carbon black, a molded article made of the conductive nylon resin composition was produced in exactly the same manner as in Example 1. There was no particular problem in the injection molding, and the molded article had sufficient conductivity in a desired shape. A molded product was easily obtained. (Comparative Example 1) The furnace method carbon black subjected to the heat treatment in Example 1 was used without heat treatment,
When a molded article made of the conductive nylon resin composition was manufactured in exactly the same manner as in Example 1, the viscosity of the resin composition was too high at the time of molding, and the molded article could not be formed into a desired shape. Also,
The volume resistivity of the molded product was also higher than that of the example. (Comparative Example 2) Table 1 shows the physical properties of carbon black obtained in exactly the same manner as in Example 1 except that air was charged at 10 L / min instead of CO 2 gas during the heat treatment. Using the obtained carbon black, a molded article made of the conductive nylon resin composition was produced in exactly the same manner as in Example 1, and the viscosity of the resin composition was too high at the time of molding, and the molded article could not be molded into a desired shape. Was. Further, the volume resistivity of the molded product was significantly higher than that of the example. (Comparative Example 3) Table 1 shows the physical properties of carbon black obtained in exactly the same manner as in Example 1 except that the heat treatment was performed at 800 ° C for 1 hour. Using the obtained carbon black, a molded product made of the conductive nylon resin composition was produced in exactly the same manner as in Example 1, and the volume resistivity of the molded product was larger than that of the example. (Comparative Example 4) Specific surface area 225 m 2 / g, DBP absorption 1
Table 1 shows the physical properties of carbon black obtained by subjecting a furnace-process carbon black having a volatile composition shown in Table 1 to a heat treatment of 61 ml / 100 g and an ash content of 0.65% in exactly the same manner as in Example 1. Using the obtained carbon black, a molded product made of the conductive nylon resin composition was produced in exactly the same manner as in Example 1, and the volume resistivity of the molded product was significantly higher than that of the example.

【0016】[0016]

【発明の効果】本発明の導電性カーボンブラックは、樹
脂に混練した場合に、加工性を保持しながら十分な導電
性を付与し得るカーボンブラックであり、帯電防止等を
必要とする安価な導電性成型品を与え得る材料として好
適である。
The conductive carbon black of the present invention is a carbon black capable of imparting sufficient conductivity while maintaining processability when kneaded with a resin. It is suitable as a material that can give a molded product.

【0017】[0017]

【表1】 [Table 1]

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 加熱処理前の全酸素量が20mg/g以
下であるファーネスブラックを、不活性雰囲気下で加熱
処理することにより、全酸素量を5〜50%低減してな
ることを特徴とする導電性カーボンブラック。
1. Furnace black having a total oxygen content of 20 mg / g or less before heat treatment is heat-treated in an inert atmosphere to reduce the total oxygen content by 5 to 50%. Conductive carbon black.
【請求項2】 前記加熱処理により、全酸素量を5〜3
0%低減してなることを特徴とする請求項1記載の導電
性カーボンブラック。
2. The heat treatment reduces the total oxygen content to 5 to 3
2. The conductive carbon black according to claim 1, wherein the carbon black is reduced by 0%.
【請求項3】 樹脂混練用であることを特徴とする請求
項1又は2記載の導電性カーボンブラック。
3. The conductive carbon black according to claim 1, which is used for kneading a resin.
JP34498997A 1997-12-15 1997-12-15 Conductive carbon black Pending JPH11172146A (en)

Priority Applications (1)

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Cited By (8)

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JP2002150843A (en) * 2000-11-08 2002-05-24 Mikuni Color Ltd Conductive plastic sheet for carrier tape
JP2006022270A (en) * 2004-07-09 2006-01-26 Mitsubishi Chemicals Corp Carbon black and method for producing the same
JP2006206780A (en) * 2005-01-28 2006-08-10 Mitsubishi Chemicals Corp Conductive thermoplastic resin composition
JP2006205464A (en) * 2005-01-26 2006-08-10 Tokai Rubber Ind Ltd Fuel hose
JP2019076082A (en) * 2017-10-23 2019-05-23 株式会社張自動化Jang Automation Co., Ltd. Seeder having static electricity release function
US10767028B2 (en) 2016-02-01 2020-09-08 Cabot Corporation Compounded rubber having improved thermal transfer
JP2021004277A (en) * 2019-06-25 2021-01-14 東海カーボン株式会社 Aqueous dispersion of conductive carbon black raw material, manufacturing method of aqueous dispersion of conductive carbon black raw material, conductive carbon black powder, manufacturing method of conductive carbon black powder and manufacturing method of positive electrode for lithium ion secondary battery
US11352536B2 (en) 2016-02-01 2022-06-07 Cabot Corporation Thermally conductive polymer compositions containing carbon black

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002150843A (en) * 2000-11-08 2002-05-24 Mikuni Color Ltd Conductive plastic sheet for carrier tape
JP2006022270A (en) * 2004-07-09 2006-01-26 Mitsubishi Chemicals Corp Carbon black and method for producing the same
JP2006205464A (en) * 2005-01-26 2006-08-10 Tokai Rubber Ind Ltd Fuel hose
JP2006206780A (en) * 2005-01-28 2006-08-10 Mitsubishi Chemicals Corp Conductive thermoplastic resin composition
US10767028B2 (en) 2016-02-01 2020-09-08 Cabot Corporation Compounded rubber having improved thermal transfer
US11352536B2 (en) 2016-02-01 2022-06-07 Cabot Corporation Thermally conductive polymer compositions containing carbon black
US11732174B2 (en) 2016-02-01 2023-08-22 Cabot Corporation Thermally conductive polymer compositions containing carbon black
US12180412B2 (en) 2016-02-01 2024-12-31 Cabot Corporation Thermally conductive polymer compositions containing carbon black
JP2019076082A (en) * 2017-10-23 2019-05-23 株式会社張自動化Jang Automation Co., Ltd. Seeder having static electricity release function
JP2021004277A (en) * 2019-06-25 2021-01-14 東海カーボン株式会社 Aqueous dispersion of conductive carbon black raw material, manufacturing method of aqueous dispersion of conductive carbon black raw material, conductive carbon black powder, manufacturing method of conductive carbon black powder and manufacturing method of positive electrode for lithium ion secondary battery

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