JPH037740A - Electroconductive thermoplastic resin composition and production thereof - Google Patents
Electroconductive thermoplastic resin composition and production thereofInfo
- Publication number
- JPH037740A JPH037740A JP1142355A JP14235589A JPH037740A JP H037740 A JPH037740 A JP H037740A JP 1142355 A JP1142355 A JP 1142355A JP 14235589 A JP14235589 A JP 14235589A JP H037740 A JPH037740 A JP H037740A
- Authority
- JP
- Japan
- Prior art keywords
- graphite
- thermoplastic resin
- resin composition
- acid
- present
- 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
Links
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- Carbon And Carbon Compounds (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Shielding Devices Or Components To Electric Or Magnetic Fields (AREA)
- Conductive Materials (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は導電性熱可塑性樹脂組成物及びその製造方法に
係り、特に帯電防止性、電磁波の遮蔽性が要求される分
野に好適な成形品成形材料として有用な導電性熱可塑性
樹脂組成物及びその製造方法に関する。Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a conductive thermoplastic resin composition and a method for producing the same, and particularly to a molded article suitable for fields where antistatic properties and electromagnetic wave shielding properties are required. The present invention relates to a conductive thermoplastic resin composition useful as a molding material and a method for producing the same.
[従来の技術]
日常の生活空間にはテレビ、ラジオなどの放送用電波の
ほか、自動車やバイラのイグニションノイズ等の高周波
ノイズ、電子レンジ等の誕電加熱装置からの漏洩電磁波
など、種々の周波数の電磁波が充満しており、これらの
電磁波がテレビやラジオ、コンピュータ端末機、医療用
機器、プロセス制御装置などに影響を与えるという問題
が発生している。[Conventional technology] In addition to broadcasting radio waves from televisions and radios, daily living spaces contain various frequencies such as high-frequency noises such as ignition noise from cars and barbers, and leakage electromagnetic waves from heating devices such as microwave ovens. The world is full of electromagnetic waves, and problems have arisen in that these electromagnetic waves affect televisions, radios, computer terminals, medical equipment, process control equipment, etc.
また、電子機器を中心とする機器類に近年多用されるプ
ラスチックは、接触摩擦等により静電気を発生、帯電し
やすいのみならず、電磁波に対しては透過性であること
から、内部の電子装置に影響を与え、種々のトラブルの
原因となりやすく、そのため静電気的障害、電磁波的障
害に対する対策が社会的に重要な問題になりつつある。In addition, plastics, which have been frequently used in electronic equipment and other equipment in recent years, are not only prone to generating static electricity and being charged due to contact friction, etc., but also are transparent to electromagnetic waves, making them difficult to protect internal electronic devices. Therefore, countermeasures against electrostatic interference and electromagnetic interference are becoming a socially important issue.
これらの静電気、電磁波による障害に対しては、従来よ
り広い産業分野において各種の試みがなされ、又研究が
なされている。Various attempts and research have been made to deal with these disturbances caused by static electricity and electromagnetic waves in a wide range of industrial fields.
一般に、帯電体の導電性を増すことにより帯電電荷が減
少し、その結果帯電しにくく、静電気的な障害を起こし
にくいものとなるが、一方、電磁波の遮蔽効果について
も、導電性の高い物体はど電波の減衰も大きく、より大
きな電磁波遮蔽効果を示す。また、一般に、電磁波障害
対策は静電気障害対策より高い導電性が必要とされる場
合が多く、最近の電磁波遮蔽材等で要求されるような低
抵抗領域の導電性であれば、同時に静電気的障害の防止
要求を満たす場合が多い。Generally, by increasing the conductivity of a charged object, the charge will be reduced, and as a result, it will become less likely to be charged and cause electrostatic disturbances.On the other hand, with regard to the shielding effect of electromagnetic waves, objects with high conductivity The attenuation of both radio waves is large, indicating a greater electromagnetic wave shielding effect. In addition, in general, countermeasures against electromagnetic interference often require higher conductivity than countermeasures against static electricity, and if the conductivity is in the low resistance range required for recent electromagnetic shielding materials, it will also prevent static electricity. In many cases, it satisfies the prevention requirements of
近年、コンピュータ等の電子機器用ハウジング等に特に
高度の電磁波遮蔽材料が要求されるようになり、導電性
の高い金、銀、銅、ニッケル、アルミニウム、鉄等の金
属類或いはカーボンブラック、グラファイト、炭素繊維
等の炭素化合物の繊維又は微粒子を利用する方法が試み
られている。In recent years, particularly advanced electromagnetic shielding materials have been required for housings for electronic devices such as computers, and highly conductive metals such as gold, silver, copper, nickel, aluminum, iron, carbon black, graphite, etc. Attempts have been made to utilize fibers or fine particles of carbon compounds such as carbon fibers.
これらのうち、銀、銅、ニッケル等の金属粉末又は黒鉛
粉末は、主としてコンピュータハウジングの電磁波シー
ルド用に使用される導電性塗料の導電性フィラーとして
利用されており、この導電性塗料は導電性フィラー、バ
インダー、溶剤、添加剤等から構成されるものであって
、塗膜形成時に導電性フィラーの鎖状連結により導電性
が発現されるものと考えられている。Among these, metal powders such as silver, copper, and nickel, or graphite powders are mainly used as conductive fillers in conductive paints used for electromagnetic shielding of computer housings. , a binder, a solvent, additives, etc., and it is thought that conductivity is developed through chain-like connections of conductive fillers during coating film formation.
[発明が解決しようとする課題]
ところで、熱可塑性樹脂、なかでも石油を素原料として
合成される熱可塑性樹脂は、その製品特性の安定性、工
業的に受は入れられやすい成形性により、家庭用或いは
工業用の電化製品、自動車の電子装置、電子機器のハウ
ジングの一部に利用される傾向がますます高まっており
、これらの熱可塑性樹脂に対して帯電防止又は電磁波遮
蔽機能を付与する技術に対する要求が年々高まっている
。[Problem to be solved by the invention] By the way, thermoplastic resins, especially thermoplastic resins synthesized using petroleum as a raw material, have become popular in the household due to their stable product characteristics and moldability that is easily accepted industrially. There is an increasing tendency for thermoplastic resins to be used in commercial and industrial electrical appliances, automobile electronic devices, and parts of the housings of electronic devices, and technology that provides antistatic or electromagnetic wave shielding functions to these thermoplastic resins. Demand for this is increasing year by year.
本発明は上記実情に鑑みてなされたものであって、熱可
塑性樹脂に高い導電性を付与することにより、優れた帯
電防止性能及び電磁波遮蔽性能を有する製品を成形する
ことができる導電性熱可塑性樹脂組成物及びその製造方
法を提供することを目的とする。The present invention has been made in view of the above circumstances, and is a conductive thermoplastic that can be molded into a product having excellent antistatic performance and electromagnetic shielding performance by imparting high conductivity to a thermoplastic resin. An object of the present invention is to provide a resin composition and a method for producing the same.
[課題を解決するための手段]
請求項(1)の導電性熱可塑性樹脂組成物は、8〜50
重量%の膨張化黒鉛粉末を含有してなることを特徴とす
る
請求項(2)の導電性熱可塑性樹脂組成物は請求項(1
)において、膨張化黒鉛粉末が、酸処理黒鉛を膨張度1
00〜300mf/gに膨張させて得られたものである
ことを特徴とする請求項(3)の導電性熱可塑性樹脂組
成物の製造方法は、酸処理黒鉛を膨張度100〜300
m It / gに膨張させて得られた膨張化黒鉛粉末
を圧縮して、密度0.05〜0.8g/crrI″の圧
縮黒鉛となした後、熱可塑性樹脂と混合、練和すること
により、上記請求項(2)の導電性熱可塑性樹脂組成物
を製造することを特徴とする。[Means for Solving the Problems] The conductive thermoplastic resin composition of claim (1) has a molecular weight of 8 to 50
The conductive thermoplastic resin composition according to claim (2), characterized in that it contains % by weight of expanded graphite powder.
), the expanded graphite powder has an expansion degree of 1 compared to acid-treated graphite.
The method for producing a conductive thermoplastic resin composition according to claim (3), wherein the conductive thermoplastic resin composition is obtained by expanding acid-treated graphite to an expansion degree of 100 to 300 mf/g.
By compressing the expanded graphite powder obtained by expanding it to mIt/g to form compressed graphite with a density of 0.05 to 0.8 g/crrI'', and then mixing and kneading it with a thermoplastic resin. , characterized in that the conductive thermoplastic resin composition of claim (2) is produced.
即ち、本発明者らは、上記本発明の目的を達成するべく
鋭意検討を重ねた結果、熱可塑性樹脂組成物に特定の黒
鉛粉末の所定量を含有させることにより、極めて高い導
電性を付与させることができることを見出し本発明を完
成させた。That is, as a result of intensive studies to achieve the above object of the present invention, the present inventors have found that extremely high conductivity can be imparted by incorporating a predetermined amount of a specific graphite powder into a thermoplastic resin composition. They discovered that it is possible to do this and completed the present invention.
以下に本発明の詳細な説明する。The present invention will be explained in detail below.
まず、本発明で用いる膨張化黒鉛について説明する。First, the expanded graphite used in the present invention will be explained.
本発明において「膨張化黒鉛」とは、後述するような急
激な加熱によって膨張した状態の黒鉛を指し、種々の方
法で調製された多種多様な組成物が挙げられるが、本発
明においては特に酸処理黒鉛を膨張度100〜300m
j2./gに膨張させて得られたものが好ましい。なお
、本発明における「酸処理黒鉛」とは、天然黒鉛、熱分
解黒鉛、キッシュ黒鉛等の黒鉛を、濃厚な硫酸と強い酸
化剤との混合物で処理した後、水洗し、乾燥して得られ
るものをいい、黒鉛シートなどの製造に用いられる工業
的な熱膨張性黒鉛は通常このものに相当する。In the present invention, "expanded graphite" refers to graphite that has been expanded by rapid heating as described below, and includes a wide variety of compositions prepared by various methods. Expansion degree of treated graphite is 100-300m
j2. It is preferable to use one obtained by expanding the amount to 1/g. In addition, "acid-treated graphite" in the present invention is obtained by treating graphite such as natural graphite, pyrolytic graphite, quiche graphite, etc. with a mixture of concentrated sulfuric acid and a strong oxidizing agent, washing with water, and drying. Industrial thermally expandable graphite used in the manufacture of graphite sheets and the like usually corresponds to this type of graphite.
この酸処理黒鉛は、黒鉛の有する層状構造の層間に硫酸
が残留、固定されているものであり、約500℃以上に
急激に加熱することにより眉間に存在する硫酸が膨張す
ることによってC軸方向に数10〜数100倍に膨張す
る性買を有するものであって、熱膨張後の黒鉛層は互い
にゆるく接している構造となっている。In this acid-treated graphite, sulfuric acid remains and is fixed between the layers of the graphite's layered structure, and when it is rapidly heated to about 500°C or higher, the sulfuric acid present between the eyebrows expands, resulting in a change in the C-axis direction. The graphite layer has the property of expanding several tens to hundreds of times over time, and the graphite layers after thermal expansion have a structure in which they are in loose contact with each other.
本発明で使用される酸処理黒鉛は、その原料黒鉛、製造
方法には特に制限はないが、その特性としては、100
0℃で10秒間、急激に加熱するときの膨張度が100
〜300 m It / gであることが望ましく、こ
のような酸処理黒鉛は、例えば、98重量%濃硫酸と6
0重量%過酸化水素水の混合物中に約20〜150メツ
シユに粉砕された黒鉛を、45℃以下で10分〜30分
接触させ、水洗、乾燥を行うことにより製造することが
できる。The acid-treated graphite used in the present invention is not particularly limited in its raw material graphite or manufacturing method, but its characteristics are as follows:
The degree of expansion when heated rapidly for 10 seconds at 0℃ is 100.
~300 mIt/g is desirable, and such acid-treated graphite is prepared, for example, by 98% by weight concentrated sulfuric acid and 6%
It can be produced by contacting graphite pulverized into about 20 to 150 meshes in a mixture of 0% by weight hydrogen peroxide at a temperature below 45° C. for 10 to 30 minutes, followed by washing with water and drying.
本発明において導電性の発現は、黒鉛片が熱可塑性樹脂
と混合され加熱されて流動状態において練和される過程
で、互いにゆるく接している黒鉛片が剥離しながら変形
し、かつ互いに部分的に結合点を持つか、又は極めて微
少な距離を保って分散されることによって、電気的な連
結回路が形成されることが主な理由と考えられる。この
ため、本発明で用いられる酸処理黒鉛の粒子径はその導
電性付与の面から、150メツシユより大きいものが望
ましく、特に100メツシユより大きいものがより好適
である。一方、粒子径が大きい場合、例えば20メツシ
ユより大きい場合には、膨張した黒鉛片の大きさとして
は十分であるが、これにより特段の導電性の向上はみら
れない。従って、本発明で使用される酸処理黒鉛の粒度
は、実用的には20〜150メツシユの範囲で分級され
ているものが好ましい。In the present invention, the development of conductivity occurs during the process in which graphite pieces are mixed with thermoplastic resin, heated, and kneaded in a fluid state, in which the graphite pieces that are loosely in contact with each other deform while peeling off, and partially form each other. The main reason is thought to be that an electrical connection circuit is formed by having connection points or being dispersed at extremely small distances. Therefore, the particle diameter of the acid-treated graphite used in the present invention is preferably larger than 150 mesh, particularly preferably larger than 100 mesh, from the viewpoint of imparting electrical conductivity. On the other hand, when the particle size is large, for example larger than 20 meshes, the expanded graphite pieces are of sufficient size, but no particular improvement in conductivity is observed. Therefore, the particle size of the acid-treated graphite used in the present invention is preferably classified in the range of 20 to 150 meshes for practical purposes.
一般に、酸処理黒鉛の粒度は、通常、これを製造する際
の原料黒鉛の粒度に左右され、従フて原料の粒度に応じ
たある範囲の粒度分布を有しており、目的によって使い
分けられている。従って、酸処理黒鉛の粒度の調整は原
料黒鉛又は酸処理黒鉛を粉砕するなどの方法で容易に行
なうことができる。In general, the particle size of acid-treated graphite usually depends on the particle size of the raw material graphite used to manufacture it, and therefore has a particle size distribution within a certain range depending on the particle size of the raw material, and can be used depending on the purpose. There is. Therefore, the particle size of acid-treated graphite can be easily adjusted by pulverizing raw graphite or acid-treated graphite.
本発明で使用される酸処理黒鉛の場合は、酸処理黒鉛の
粒度と膨張度及び膨張化黒鉛粉末の嵩密度とは概ね関連
があり、通常、150メツシユ〜100メツシユの粒度
の酸処理黒鉛については膨張度が100〜160mJZ
/gで嵩密度は0.01〜0.0063g/mIt、1
00〜40メツシユの粒度のものについては膨張度13
0〜250 m 42 / gで嵩密度0.0077〜
0.004g/mJ2.40〜20メツシユの粒度のも
のについては膨張度200〜300mIt/gで嵩密度
0. OO5〜O,OO3g/mltとなる。このよ
うなことから、本発明で用いられる酸処理黒鉛の膨張度
は100〜300mA/gであることが好ましい。In the case of the acid-treated graphite used in the present invention, there is a general relationship between the particle size and expansion degree of the acid-treated graphite and the bulk density of the expanded graphite powder, and usually for acid-treated graphite with a particle size of 150 to 100 mesh. The degree of expansion is 100-160mJZ
/g and the bulk density is 0.01-0.0063g/mIt, 1
For particles with a mesh size of 00 to 40, the expansion degree is 13.
Bulk density 0.0077~ at 0~250 m42/g
For particles with a particle size of 0.004 g/mJ2.40 to 20 mesh, the swelling degree is 200 to 300 mIt/g and the bulk density is 0. OO5~O, OO3g/mlt. For this reason, the degree of expansion of the acid-treated graphite used in the present invention is preferably 100 to 300 mA/g.
本発明において使用される膨張化黒鉛粉末は、前記の粒
度分布を有している酸処理黒鉛を500℃以上、好まし
くは700〜1500℃で数秒間、更に好ましくは80
0〜1100℃で2〜5秒間加熱することにより熱膨張
させて得られる。The expanded graphite powder used in the present invention is prepared by heating acid-treated graphite having the above-mentioned particle size distribution at 500°C or higher, preferably at 700 to 1500°C for several seconds, and more preferably at 80°C.
It is obtained by thermal expansion by heating at 0 to 1100°C for 2 to 5 seconds.
この場合、熱膨張は、例えば所定の温度に制御された電
気炉内又はガスバーナー炉に連続的に酸処理黒鉛を供給
することにより、工業的な規模で実施することが出来る
。In this case, thermal expansion can be carried out on an industrial scale, for example, by continuously feeding the acid-treated graphite into an electric furnace or gas burner furnace controlled at a predetermined temperature.
なお、ここでいう「膨張度」とは、1000℃に保持さ
れた電気炉内に10分以上保持して加熱された150c
cの石英ビー力を炉外に取り出し、直ちに酸処理黒鉛o
、5gを投入し、同じく1000℃に保持された炉中に
素早く入れ、そのまま10秒間保持した後、炉外に取り
出し、自然冷却の後に、ビー力に付した目盛りによって
、膨張後の黒鉛層の上部位置を読み取って容積を測定し
、算出する値(単位:+nQ/g)をいう。In addition, the "degree of expansion" here refers to 150℃ heated by holding it in an electric furnace maintained at 1000℃ for 10 minutes or more.
Take out the quartz bead of c to the outside of the furnace and immediately add acid-treated graphite o.
, 5g was put into the furnace which was also maintained at 1000°C, held for 10 seconds, taken out of the furnace, and allowed to cool naturally. This is the value (unit: +nQ/g) calculated by reading the upper position and measuring the volume.
また、「嵩密度」は、上記膨張度の逆数(単位: g/
mJ2)で定義され、膨張度の測定を行えば直ちに算定
されるが、次のような方法でも測定することができる。In addition, "bulk density" is the reciprocal of the degree of expansion (unit: g/
mJ2), and can be calculated immediately by measuring the degree of expansion, but it can also be measured by the following method.
即ち、膨張炉から排出される膨張化黒鉛粉末の適量を静
かに1000mftのメスシリンダーに移し、直ちにメ
スシリンダーの上部をラップフィルムなどで覆って一畳
夜室温で静置する。静置させた後の容積を読み取り、一
方、膨張化黒鉛粉末の重量を別途測定して嵩密度を求め
る。That is, an appropriate amount of expanded graphite powder discharged from the expansion furnace is gently transferred to a 1000 mft graduated cylinder, the top of the graduated cylinder is immediately covered with a cling film, and the cylinder is left to stand overnight at room temperature. The volume after being allowed to stand is read, and the weight of the expanded graphite powder is separately measured to determine the bulk density.
酸処理黒鉛の膨張度が100mぶ75未満の場合は黒鉛
のC軸方向への膨張が十分でなく、その結果、酸処理黒
鉛の層間剥離が十分に行なわれず、このような膨張化黒
鉛を樹脂に添加しても、C軸方向の厚さの大きな、即ち
、剥離しない重層のままの度素粒子が樹脂中に存在する
ことになる。このため、樹脂中に分散される黒鉛粉末の
粒子数が少なくなり、黒鉛粉末による鎖状連結の形成が
不十分となり、電気的な連結回路の形成も十分でなく、
導電性の改善効果が期待できない。If the degree of expansion of the acid-treated graphite is less than 100m/75, the expansion of the graphite in the C-axis direction is insufficient, and as a result, the delamination of the acid-treated graphite is not sufficiently performed, and such expanded graphite is Even if it is added to the resin, there will be particles with a large thickness in the C-axis direction, that is, particles that do not peel off and remain in a multilayered state, in the resin. For this reason, the number of graphite powder particles dispersed in the resin decreases, the formation of chain connections by the graphite powder becomes insufficient, and the formation of electrical connection circuits is also insufficient.
No improvement in conductivity can be expected.
方、酸処理黒鉛の膨張度が300 m i/ gを超え
ても、導電性付与に関してはそれに見合う効果が期待で
きず、また、このような膨張化黒鉛粉末を工業的に製造
することは極めて困難であり、経済的見地から実用的で
はない。On the other hand, even if the degree of expansion of acid-treated graphite exceeds 300 m i/g, no corresponding effect can be expected in terms of imparting conductivity, and it is extremely difficult to industrially produce such expanded graphite powder. difficult and impractical from an economic standpoint.
一方、本発明の熱可塑性樹脂組成物を構成する熱可塑性
樹脂としては特に制限はなく、例えばポリエチレン、ポ
リプロピレン、ポリブチレン及びこれらのモノマーと酢
酸ビニル、アクリル酸エステルどの共重合体等のポリオ
レフィン樹脂類、ポリ塩化ビニル樹脂類、ポリスチレン
、アクリロニトリル−スチレン共重合体、アクリロニト
リル−ブタジェン−スチレン共重合体等のポリスチレン
系樹脂類、ポリエチレンテレフタレート等のポリエステ
ル系樹脂類、ナイロン等のポリアミド系樹脂類、ポリオ
キシメチレン等のエーテル系樹脂類の他、塩素化ポリエ
チレン、ポリブタジェン、ポリイソプレン等のエラスト
マー類等を代表的なものとして挙げることができる。On the other hand, the thermoplastic resin constituting the thermoplastic resin composition of the present invention is not particularly limited, and includes, for example, polyolefin resins such as polyethylene, polypropylene, polybutylene, and copolymers of these monomers with vinyl acetate, acrylic ester, etc. Polyvinyl chloride resins, polystyrene, polystyrene resins such as acrylonitrile-styrene copolymer, acrylonitrile-butadiene-styrene copolymer, polyester resins such as polyethylene terephthalate, polyamide resins such as nylon, polyoxymethylene In addition to ether resins such as ether resins, elastomers such as chlorinated polyethylene, polybutadiene, and polyisoprene can be cited as representative examples.
本発明において、熱可塑性樹脂に対する膨張化黒鉛粉末
の添加比率は、熱可塑性樹脂組成物中の含有量として8
〜50重量%、より好ましくは10〜40重量%となる
ように設定する。膨張化黒鉛の含有量が8重量%より少
ない場合は、黒鉛片同士の連結が不十分となり、所望の
導電性が発揮されず、また、50重量%より多くてもそ
れに見合う導電性の向上が認められない上に、得られる
成形品の特性を低下させるなどの不具合がある。In the present invention, the addition ratio of expanded graphite powder to the thermoplastic resin is 8 as the content in the thermoplastic resin composition.
The content is set to 50% by weight, more preferably 10 to 40% by weight. If the content of expanded graphite is less than 8% by weight, the graphite pieces will not be sufficiently connected to each other, and the desired conductivity will not be achieved, and if the content is more than 50% by weight, the conductivity will not improve commensurately. Not only is this not acceptable, but it also causes problems such as deteriorating the properties of the resulting molded product.
1
なお、本発明の導電性熱可塑性樹脂組成物においては、
通常のプラスチック製品に使用される一般的な添加剤、
即ち、酸化防止剤、帯電防止剤、滑剤、架橋剤、難燃剤
、染顔料、導電性フィラー、充填剤等が添加、配合され
ていても良いことは言うまでもない。1 In addition, in the conductive thermoplastic resin composition of the present invention,
Common additives used in ordinary plastic products,
That is, it goes without saying that antioxidants, antistatic agents, lubricants, crosslinking agents, flame retardants, dyes and pigments, conductive fillers, fillers, etc. may be added or blended.
次に、本発明の導電性熱可塑性樹脂組成物を製造する方
法について説明する。Next, a method for manufacturing the conductive thermoplastic resin composition of the present invention will be explained.
本発明の導電性熱可塑性樹脂組成物を製造する方法とし
ては、熱可塑性樹脂原料と所定量の膨張化黒鉛粉末、更
に必要に応じて各M添加剤を、ヘンシェルミキサー リ
ボンブレンダー等通常使用される混合装置によって攪拌
混合し、次いで単軸又は二軸スクリュー押出機、ニーダ
−、バンバリーミキサ−等通常使用される混練機で混練
するか、あるいは、加熱三木ロール等を使用して練和す
る方法を挙げることができる。As a method for manufacturing the conductive thermoplastic resin composition of the present invention, a thermoplastic resin raw material, a predetermined amount of expanded graphite powder, and, if necessary, each M additive are mixed using a Henschel mixer, ribbon blender, etc. The mixture is stirred and mixed using a mixing device, and then kneaded using a commonly used kneading machine such as a single or twin screw extruder, kneader, or Banbury mixer, or kneaded using a heated Miki roll or the like. can be mentioned.
練和する際の温度条件としては、使用する熱可塑性樹脂
原料の融点以上、融点+100℃程度以下の温度を挙げ
ることができるが、一般に膨張性 2
黒鉛粉末の添加により混合物の流動性が低下する傾向が
あるので融点+30℃以上で練和することがより有利で
あり、上限温度は、通常、熱可塑性樹脂の熱安定性によ
って決定される。Temperature conditions during kneading include temperatures above the melting point of the thermoplastic resin raw material used and below the melting point +100°C, but in general, the fluidity of the mixture decreases due to the addition of expandable graphite powder. Therefore, it is more advantageous to knead at a temperature above the melting point +30°C, and the upper limit temperature is usually determined by the thermal stability of the thermoplastic resin.
更に膨張化黒鉛粉末を添加する際の有利な方法としては
、請求項(3)の方法、即ち、酸処理黒鉛を膨張度10
0〜300mJL/gに膨張させて得られた膨張化黒鉛
粉末を加圧、圧縮して、0.05〜0.8g/cゴ、好
ましくは0.1〜0.4g/crr?の圧縮黒鉛となし
た後、熱可塑性樹脂原料と混合し、ついで練和する方法
を挙げることができる。即ち、本発明で用いる膨張化黒
鉛は極めて高い潤滑性を有していて滑り易いため、溶融
樹脂へのくい込みが悪いこと、樹脂原料と比較して嵩高
さが大きすぎるため樹脂中への添加時ないし練和時の作
業性が良好でなく、樹脂中への分散性が損なわれること
がある。このため、圧縮黒鉛とした状態で添加するのが
好ましい。この際、圧縮黒鉛の密度が0.05g/ct
rl″未満では作業性が十分改善されず、密度が0.8
g/cm3を超えると黒鉛粒子の解離が遅くなり、樹脂
への分散性が低下するので望ましくない。このように圧
縮された黒鉛は0.5〜5mm四方の大きさに容易に解
砕でき、混練機への供給が容易であるばかりでなく、短
い混練時間で樹脂中に十分に分散することができる。Furthermore, an advantageous method for adding expanded graphite powder is the method of claim (3), that is, adding acid-treated graphite to an expansion degree of 10.
The expanded graphite powder obtained by expanding it to 0 to 300 mJL/g is pressurized and compressed to give a powder of 0.05 to 0.8 g/c, preferably 0.1 to 0.4 g/crr. After forming compressed graphite, it is mixed with a thermoplastic resin raw material and then kneaded. That is, the expanded graphite used in the present invention has extremely high lubricity and is slippery, so it does not penetrate into the molten resin easily, and it is too bulky compared to the resin raw material, so it is difficult to add it to the resin. Otherwise, the workability during kneading is not good, and the dispersibility in the resin may be impaired. For this reason, it is preferable to add it in the form of compressed graphite. At this time, the density of compressed graphite is 0.05 g/ct
If it is less than rl'', the workability will not be improved sufficiently and the density will be 0.8.
If it exceeds g/cm3, the dissociation of the graphite particles will be delayed and the dispersibility in the resin will be reduced, which is not desirable. Graphite compressed in this way can be easily crushed into a size of 0.5 to 5 mm square, and not only can it be easily fed to a kneader, but it can also be sufficiently dispersed in the resin in a short kneading time. can.
本発明の導電性熱可塑性樹脂組成物は、直接押出しシー
ト、射出成形品などの成形品とすることもできる他、発
泡剤を添加して発泡成形品として使用することもできる
。更に、マスターバッチ、コンパウンドとしてその他の
熱可塑性樹脂類による希釈、あるいは混合により成形品
に供することもできる。いずれの場合においても、膨張
化黒鉛粉末の配合量は所望の導電性に応じて、本発明の
範囲内で自由に設定できることは言うまでもない。The conductive thermoplastic resin composition of the present invention can be made into molded products such as directly extruded sheets and injection molded products, and can also be used as foam molded products by adding a foaming agent. Furthermore, it can be diluted with other thermoplastic resins as a masterbatch or compound, or mixed with other thermoplastic resins to form molded products. In either case, it goes without saying that the amount of expanded graphite powder to be added can be freely set within the scope of the present invention depending on the desired conductivity.
本発明の導電性熱可塑性樹脂組成物或いはこれを成形し
て得られる成形品については、更に、表面の美装化、耐
水化、難燃化等を目的として異種材料との組合せによる
複合材料とすることも可能である。The conductive thermoplastic resin composition of the present invention or a molded article obtained by molding the same may be further used as a composite material by combining different materials for the purpose of aestheticizing the surface, making it water resistant, making it flame retardant, etc. It is also possible to do so.
[作用]
熱膨張によりC軸方向に高度に膨張し、黒鉛層が互いに
ゆるく接している構造とされた膨張化黒鉛は、その黒鉛
片が熱可塑性樹脂と混合され加熱されて流動状態におい
て練和される過程で、剥離しながら変形し、かつ互いに
部分的に結合点を持つか、又は極めて微少な距離を保っ
て分散された状態となる。このため、樹脂組成物内の膨
張化黒鉛部分に電気的な連結回路が形成されて良好な導
電性が発現される。[Function] Expanded graphite is highly expanded in the C-axis direction due to thermal expansion and has a structure in which the graphite layers are loosely in contact with each other.The graphite pieces are mixed with a thermoplastic resin, heated, and kneaded in a fluid state. In the process of being separated, they deform while exfoliating, and either have partial bonding points with each other, or become dispersed with extremely small distances between them. Therefore, an electrical connection circuit is formed in the expanded graphite portion within the resin composition, and good electrical conductivity is exhibited.
なお、膨張化黒鉛粉末は極めて軽量であるため、製品の
軽量化にも有効である。In addition, since expanded graphite powder is extremely lightweight, it is also effective in reducing the weight of products.
特に、請求項(2)によれば、著しく導電性に優れた導
電性熱可塑性樹脂組成物が提供される。In particular, according to claim (2), a conductive thermoplastic resin composition having extremely excellent conductivity is provided.
しかして、このような導電性熱可塑性樹脂組成物は、請
求項(3)の方法により工業的に有利に製造される。Therefore, such a conductive thermoplastic resin composition can be advantageously produced industrially by the method of claim (3).
[実施例]
5
以下に製造例、実施例及び比較例を挙げて本発明をより
具体的に説明するが、本発明はその要旨を超えない限り
、以下の実施例に限定されるものではない。[Example] 5 The present invention will be explained in more detail with reference to production examples, working examples, and comparative examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof. .
なお、製造例、実施例及び比較例において、「部」は1
1部」を、1%」は「重量%」を示す。In addition, in production examples, working examples, and comparative examples, "part" is 1
"1 part" indicates "% by weight" and "1%" indicates "% by weight".
製造例1:膨張化黒鉛粉末の製造
固定炭素分90%、灰分8%のカナダ産出の天然鱗片状
黒鉛〔粒度;36メツシユ〜80メツシユ〕の40部を
98%硫酸150部、60%過酸化水素水2部の混合液
に加えて、30〜35℃で15分間反応させた。次いで
反応物に150部の30%硫酸を加えて希釈した後、ガ
ラス繊維濾紙(GAloo)を用いてヌッチェで吸引濾
過し残漬を取り出した。この濾過残漬を500部の水中
に投入し、30秒間かき混ぜ洗浄した後、再び吸引濾過
により残渣を分離した。このときの残漬を再び500部
の水中に投入し、30秒間かき混ぜ洗浄した後、同様に
吸引濾過して残渣を分取し 6
た。Production Example 1: Production of Expanded Graphite Powder 40 parts of natural flaky graphite produced in Canada (particle size: 36 mesh to 80 mesh) with fixed carbon content of 90% and ash content of 8% were mixed with 150 parts of 98% sulfuric acid and 60% peroxide. It was added to a mixture of 2 parts of hydrogen water and reacted at 30 to 35°C for 15 minutes. Next, the reaction product was diluted by adding 150 parts of 30% sulfuric acid, and then suction filtered using a Nutsche filter using glass fiber filter paper (GAloo) to remove the residue. This filtered residue was poured into 500 parts of water, stirred and washed for 30 seconds, and then the residue was separated by suction filtration again. The residue was poured into 500 parts of water again, stirred and washed for 30 seconds, and then filtered with suction in the same manner to separate the residue.
次いでこの濾過残漬を105℃の熱風循環式乾燥量中で
約90分乾燥して酸処理黒鉛Aを得た。Next, this filtered residue was dried for about 90 minutes in a hot air circulating dryer at 105° C. to obtain acid-treated graphite A.
この酸処理黒鉛Aの1000℃、10秒間の膨張度の測
定結果は190mJ2/gであった。The expansion degree of this acid-treated graphite A at 1000°C for 10 seconds was 190 mJ2/g.
熱可塑性樹脂に添加、練和するために、この酸処理黒鉛
Aを別途1100℃に設定した縦型電気炉に約2秒間の
滞留時間で落下させて膨張化黒鉛粉末Aを得た。このも
のを静かに1000mλのメスシリンダーに移して、容
積と重量から求めた嵩密度は0.0055 g/m℃で
あった。In order to add and knead the thermoplastic resin, this acid-treated graphite A was separately dropped into a vertical electric furnace set at 1100°C for a residence time of about 2 seconds to obtain expanded graphite powder A. This material was gently transferred to a 1000 mλ graduated cylinder, and the bulk density determined from the volume and weight was 0.0055 g/m°C.
製造例2: ′張化黒鉛粉末の製造
固定炭素分92%、灰分6%のカナダ産出の天然鱗片状
黒鉛(粒度;60メツシユ〜100メツシユ)を用いた
こと以外は製造例1と同様の操作を行い、酸処理黒鉛B
を得た。この酸処理黒鉛Bの1000℃、10秒間の膨
張度の測定結果は140ml1.7gであった。Production Example 2: 'Production of Tensioned Graphite Powder The same procedure as Production Example 1 was used except that natural flaky graphite produced in Canada (particle size: 60 mesh to 100 mesh) with fixed carbon content of 92% and ash content of 6% was used. and acid-treated graphite B
I got it. The expansion degree of this acid-treated graphite B at 1000° C. for 10 seconds was measured to be 1.7 g in 140 ml.
熱可塑性樹脂に添加、練和するために、この酸処理黒鉛
Bを別途800℃に設定した縦型電気炉に約2秒間の滞
留時間で落下させて膨張化黒鉛粉末Bを得た。このもの
を静かに10100Oのメスシリンダーに移して、容積
と重量から求めた嵩密度は0.010g/mJ2であっ
た。In order to add and knead the thermoplastic resin, this acid-treated graphite B was separately dropped into a vertical electric furnace set at 800° C. with a residence time of about 2 seconds to obtain expanded graphite powder B. This material was gently transferred to a graduated cylinder at 10100O, and the bulk density determined from the volume and weight was 0.010 g/mJ2.
製造例3:I紅U且11
製造例1.2で得られた膨張化黒鉛粉末A、 Bを、そ
れぞれプレスにより常温で圧締して厚みがおよそ3mm
の圧縮黒鉛を得、次いでこの圧縮黒鉛をおよそ2〜5m
m四方の大きさの凝集物に解砕した。なお、この圧縮黒
鉛の密度は第1表に示す通りである。Production Example 3: I-Ku U and 11 Expanded graphite powders A and B obtained in Production Example 1.2 were compressed using a press at room temperature to a thickness of approximately 3 mm.
of compressed graphite is obtained, and then this compressed graphite is approximately 2 to 5 m long.
It was crushed into aggregates of m square size. Note that the density of this compressed graphite is as shown in Table 1.
実施例1〜8、比較例1
製造例3で得られた圧縮黒鉛と第1表に示す熱可塑性樹
脂とを第1表に示す配合で混合し、下記■の練和方法に
より熱可塑性樹脂組成物を製造した。得られた熱可塑性
樹脂組成物を用いて下記■のシート化方法によりシート
を製造し、その体積抵抗率を下記■の方法により測定し
た。結果を第1表に示す。Examples 1 to 8, Comparative Example 1 The compressed graphite obtained in Production Example 3 and the thermoplastic resin shown in Table 1 were mixed in the formulation shown in Table 1, and the thermoplastic resin composition was prepared by the kneading method described in (1) below. manufactured something. Using the obtained thermoplastic resin composition, a sheet was manufactured by the sheet-forming method described in (1) below, and the volume resistivity of the sheet was measured by the method (2) below. The results are shown in Table 1.
■ 練和方法
ブラベンダー社製「ブラベンダープラスチコーダー」の
ミキシングチャンバーを温度180℃、回転数3Orp
mに設定し、このチャンバーに、第1表に示す配合量の
熱可塑性樹脂を入れ、樹脂が流動状態で練和され始めた
状態になってから、引続き第1表に示す配合量の膨張化
黒鉛を圧縮して得られた圧縮黒鉛を10秒を要して添加
した。■ Kneading method: Use the mixing chamber of Brabender's "Brabender Plasticorder" at a temperature of 180°C and a rotation speed of 3 Orp.
m, put the thermoplastic resin in the amount shown in Table 1 into this chamber, and after the resin begins to be kneaded in a fluid state, continue to expand the amount shown in Table 1. Compressed graphite obtained by compressing graphite was added over a period of 10 seconds.
膨張化黒鉛の添加を開始してから、同じ条件に保持して
混練操作を10分間続けた。時間の測定開始後3分経過
してから、チャンバー内の混合物の温度を測定したとこ
ろ182℃であり、混練操作中殆ど設定値に近い温度を
示していた。10分間の混練が終了した後、チャンバー
より混合物を取り出した。After starting the addition of expanded graphite, the kneading operation was continued for 10 minutes while maintaining the same conditions. Three minutes after the start of time measurement, the temperature of the mixture in the chamber was measured and found to be 182° C., which was close to the set value during the kneading operation. After kneading for 10 minutes, the mixture was taken out from the chamber.
■ シート化方法
■の練和時の設定温度+20℃に予め設定された熱プレ
ス装置に、120mmX120mmx1mmの金属製の
スペーサーを設置し、■の練和操作の終了した混合物1
4部を100 k g / c m’で3分間加熱圧締
し、ついで解圧してシートを得9
た。このシートは、目視観察後、体積抵抗率測定用に1
0100mmX100に裁断した。■ Sheeting method: A metal spacer of 120 mm x 120 mm x 1 mm is installed in a heat press device preset at the temperature set during kneading in ■ + 20°C, and mixture 1 after the kneading operation in ■ is installed.
Four parts were heated and pressed at 100 kg/cm' for 3 minutes, and then the pressure was released to obtain a sheet. After visual observation, this sheet was used for volume resistivity measurement.
It was cut into a size of 100 mm x 100 mm.
■ 体積抵抗率の測定
JIS−に6911.5・13「抵抗率」に準じて測定
した。(2) Measurement of volume resistivity It was measured according to JIS-6911.5.13 "Resistivity".
比較例2〜4
第1表に示す熱可塑性樹脂を用い、圧縮黒鉛を配合しな
かったこと以外は実施例1と同様にしてシート化及び体
積抵抗率の測定を行ない、結果を第1表に示した。Comparative Examples 2 to 4 The thermoplastic resin shown in Table 1 was used, and the sheeting and volume resistivity were measured in the same manner as in Example 1, except that compressed graphite was not blended, and the results are shown in Table 1. Indicated.
比較例5.6
圧縮黒鉛の代りに第1表に示す黒鉛粉末を用いたこと以
外は実施例2と同様にして練和、シート化及び体積抵抗
率の測定を行ない、結果を第1表に示した。Comparative Example 5.6 Kneading, forming into a sheet, and measuring volume resistivity were carried out in the same manner as in Example 2, except that graphite powder shown in Table 1 was used instead of compressed graphite, and the results are shown in Table 1. Indicated.
比較例7
製造例1で得られた膨張化黒鉛を圧縮せずに用いた以外
は実施例3と同様にしてシート化及び体積抵抗率の測定
を行ない、結果を第1表に示した。本例では黒鉛粉末の
樹脂への添加に7分を要0
した。Comparative Example 7 A sheet was formed and the volume resistivity was measured in the same manner as in Example 3 except that the expanded graphite obtained in Production Example 1 was used without being compressed. The results are shown in Table 1. In this example, it took 7 minutes to add graphite powder to the resin.
第1表の結果から、本発明の範囲よりも少ない圧縮黒鉛
を配合したもの(比較例1)、圧縮黒鉛を全く配合して
いないもの(比較例2〜4)或いは圧縮していない膨張
化黒鉛を配合したもの(比較例7)では、高い体積抵抗
率を示すのに対し、本発明の導電性熱可塑性樹脂組成物
より得られるシートは極めて高い導電性を有しているこ
とが肥められる。一方、膨張化黒鉛の製造原料として使
用した天然黒鉛粉末を配合したもの(比較例56)では
殆ど導電性の向上効果は得られない。From the results in Table 1, it can be seen that those containing less compressed graphite than the range of the present invention (Comparative Example 1), those containing no compressed graphite at all (Comparative Examples 2 to 4), or those containing expanded graphite that is not compressed. (Comparative Example 7) shows a high volume resistivity, whereas the sheet obtained from the conductive thermoplastic resin composition of the present invention has extremely high conductivity. . On the other hand, in the case of blending natural graphite powder used as a raw material for producing expanded graphite (Comparative Example 56), hardly any effect of improving conductivity can be obtained.
[発明の効果]
以上詳述した通り、本発明の導電性熱可塑性樹脂組成物
によれば、著しく高い導電性を有する熱可塑性樹脂組成
物が提供される。このため、本発明の導電性熱可塑性樹
脂組成物によれば、電気製品、電子製品のキャビネット
等として有用な、優れた帯電防止効果及び電磁波遮蔽効
果を有する熱可塑性樹脂成形品が提供される。しかも、
本発明で使用される膨張化黒鉛粉末は極めて軽量である
ことから、製品の軽量化も図れる。[Effects of the Invention] As detailed above, the conductive thermoplastic resin composition of the present invention provides a thermoplastic resin composition having extremely high conductivity. Therefore, according to the conductive thermoplastic resin composition of the present invention, a thermoplastic resin molded article having excellent antistatic effect and electromagnetic wave shielding effect, which is useful as cabinets for electrical products and electronic products, is provided. Moreover,
Since the expanded graphite powder used in the present invention is extremely lightweight, it is possible to reduce the weight of the product.
特に、請求項(2)の導電性熱可塑性樹脂組成物によれ
ば、導電性により優れた熱可塑性樹脂組成物が提供され
る。In particular, according to the conductive thermoplastic resin composition of claim (2), a thermoplastic resin composition with more excellent conductivity is provided.
しかして、このような導電性熱可塑性樹脂組成物は、請
求項(3)の方法により容易に製造される。Therefore, such a conductive thermoplastic resin composition can be easily produced by the method of claim (3).
Claims (3)
化黒鉛粉末を含有してなることを特徴とする導電性熱可
塑性樹脂組成物。(1) A conductive thermoplastic resin composition characterized by containing 8 to 50% by weight of expanded graphite powder in the thermoplastic resin composition.
〜300ml/gに膨張させて得られたものであること
を特徴とする特許請求の範囲第1項に記載の導電性熱可
塑性樹脂組成物。(2) Expanded graphite powder expands acid-treated graphite to an expansion degree of 100.
The conductive thermoplastic resin composition according to claim 1, which is obtained by expanding the composition to 300 ml/g.
膨張させて得られた膨張化黒鉛粉末を圧縮して、密度0
.05〜0.8g/cm^3の圧縮黒鉛となした後、熱
可塑性樹脂と混合、練和することを特徴とする特許請求
の範囲第2項に記載の導電性熱可塑性樹脂組成物の製造
方法。(3) Expanded graphite powder obtained by expanding acid-treated graphite to an expansion degree of 100 to 300 ml/g is compressed to obtain a powder with a density of 0.
.. 05 to 0.8 g/cm^3 of compressed graphite, and then mixed and kneaded with a thermoplastic resin. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1142355A JPH037740A (en) | 1989-06-05 | 1989-06-05 | Electroconductive thermoplastic resin composition and production thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1142355A JPH037740A (en) | 1989-06-05 | 1989-06-05 | Electroconductive thermoplastic resin composition and production thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH037740A true JPH037740A (en) | 1991-01-14 |
Family
ID=15313447
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1142355A Pending JPH037740A (en) | 1989-06-05 | 1989-06-05 | Electroconductive thermoplastic resin composition and production thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH037740A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4958410A (en) * | 1988-03-23 | 1990-09-25 | Metalquima, S.A. | Machine for meat treatment and maceration with automatic loading and unloading |
| EP0787784A3 (en) * | 1996-01-31 | 1997-08-27 | Schneider Friedhelm | |
| US5776372A (en) * | 1995-05-29 | 1998-07-07 | Nisshinbo Industries, Inc. | Carbon composite material |
| JP2004250643A (en) * | 2003-02-21 | 2004-09-09 | Misato Kk | Electromagnetic wave absorption structure and method for producing the same |
| JP2013535402A (en) * | 2010-08-11 | 2013-09-12 | ティムカル ソシエテ アノニム | Grinding expanded graphite agglomerate, method for producing the same, and use thereof |
-
1989
- 1989-06-05 JP JP1142355A patent/JPH037740A/en active Pending
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4958410A (en) * | 1988-03-23 | 1990-09-25 | Metalquima, S.A. | Machine for meat treatment and maceration with automatic loading and unloading |
| US5776372A (en) * | 1995-05-29 | 1998-07-07 | Nisshinbo Industries, Inc. | Carbon composite material |
| EP0787784A3 (en) * | 1996-01-31 | 1997-08-27 | Schneider Friedhelm | |
| JP2004250643A (en) * | 2003-02-21 | 2004-09-09 | Misato Kk | Electromagnetic wave absorption structure and method for producing the same |
| JP2013535402A (en) * | 2010-08-11 | 2013-09-12 | ティムカル ソシエテ アノニム | Grinding expanded graphite agglomerate, method for producing the same, and use thereof |
| KR20130138737A (en) * | 2010-08-11 | 2013-12-19 | 팀칼 에스에이(팀칼아게)(팀칼리미티드) | Ground expanded graphite agglomerates, methods of making, and applications of the same |
| US9187612B2 (en) | 2010-08-11 | 2015-11-17 | Imerys Graphite & Carbon Switzerland Sa | Ground expanded graphite agglomerates, methods of making, and applications of the same |
| US9527740B2 (en) | 2010-08-11 | 2016-12-27 | Imerys Graphite & Carbon Switzerland Sa | Ground expanded graphite agglomerates, methods of making, and applications of the same |
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