JPS6054348B2 - Method for manufacturing high-strength plastic molded products suitable for electrodes and conductors - Google Patents
Method for manufacturing high-strength plastic molded products suitable for electrodes and conductorsInfo
- Publication number
- JPS6054348B2 JPS6054348B2 JP56007144A JP714481A JPS6054348B2 JP S6054348 B2 JPS6054348 B2 JP S6054348B2 JP 56007144 A JP56007144 A JP 56007144A JP 714481 A JP714481 A JP 714481A JP S6054348 B2 JPS6054348 B2 JP S6054348B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- graphite powder
- weight
- molding machine
- particle size
- 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
Links
- 238000000034 method Methods 0.000 title claims description 23
- 229920003023 plastic Polymers 0.000 title claims description 15
- 239000004033 plastic Substances 0.000 title claims description 15
- 239000004020 conductor Substances 0.000 title claims description 14
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 111
- 229920005989 resin Polymers 0.000 claims description 48
- 239000011347 resin Substances 0.000 claims description 48
- 238000002156 mixing Methods 0.000 claims description 38
- 239000002245 particle Substances 0.000 claims description 38
- 229920005992 thermoplastic resin Polymers 0.000 claims description 27
- -1 alkane group hydrocarbon Chemical class 0.000 claims description 26
- 239000012778 molding material Substances 0.000 claims description 23
- 239000000843 powder Substances 0.000 claims description 23
- 238000000465 moulding Methods 0.000 claims description 22
- 230000005484 gravity Effects 0.000 claims description 21
- 238000010438 heat treatment Methods 0.000 claims description 20
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 18
- 238000000748 compression moulding Methods 0.000 claims description 17
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 16
- 238000001125 extrusion Methods 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 15
- 239000002131 composite material Substances 0.000 claims description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 12
- 239000004215 Carbon black (E152) Substances 0.000 claims description 10
- 229930195733 hydrocarbon Natural products 0.000 claims description 10
- CRSOQBOWXPBRES-UHFFFAOYSA-N neopentane Chemical compound CC(C)(C)C CRSOQBOWXPBRES-UHFFFAOYSA-N 0.000 claims description 10
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims description 10
- PFEOZHBOMNWTJB-UHFFFAOYSA-N 3-methylpentane Chemical compound CCC(C)CC PFEOZHBOMNWTJB-UHFFFAOYSA-N 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 229930182556 Polyacetal Natural products 0.000 claims description 7
- 239000004743 Polypropylene Substances 0.000 claims description 7
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 claims description 7
- 229920013716 polyethylene resin Polymers 0.000 claims description 7
- 229920006324 polyoxymethylene Polymers 0.000 claims description 7
- 229920001155 polypropylene Polymers 0.000 claims description 7
- 239000000344 soap Substances 0.000 claims description 7
- 239000004925 Acrylic resin Substances 0.000 claims description 6
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 6
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 6
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 6
- 229920001225 polyester resin Polymers 0.000 claims description 6
- 239000004645 polyester resin Substances 0.000 claims description 6
- 229920005749 polyurethane resin Polymers 0.000 claims description 6
- 229910052708 sodium Inorganic materials 0.000 claims description 5
- 239000011734 sodium Substances 0.000 claims description 5
- 239000004094 surface-active agent Substances 0.000 claims description 5
- 125000001931 aliphatic group Chemical group 0.000 claims description 4
- 238000004898 kneading Methods 0.000 claims description 4
- RSWGJHLUYNHPMX-UHFFFAOYSA-N 1,4a-dimethyl-7-propan-2-yl-2,3,4,4b,5,6,10,10a-octahydrophenanthrene-1-carboxylic acid Chemical compound C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 claims description 3
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 claims 1
- 229920006026 co-polymeric resin Polymers 0.000 claims 1
- 229910002804 graphite Inorganic materials 0.000 description 24
- 239000010439 graphite Substances 0.000 description 24
- 239000006185 dispersion Substances 0.000 description 7
- 238000009736 wetting Methods 0.000 description 6
- 238000001746 injection moulding Methods 0.000 description 5
- 239000006229 carbon black Substances 0.000 description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- 210000003296 saliva Anatomy 0.000 description 3
- 229920000297 Rayon Polymers 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000314 lubricant Substances 0.000 description 2
- 239000011812 mixed powder Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- AFABGHUZZDYHJO-UHFFFAOYSA-N 2-Methylpentane Chemical compound CCCC(C)C AFABGHUZZDYHJO-UHFFFAOYSA-N 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- 229920005497 Acrypet® Polymers 0.000 description 1
- 229920001342 Bakelite® Polymers 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 238000000071 blow moulding Methods 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- MOTZDAYCYVMXPC-UHFFFAOYSA-N dodecyl hydrogen sulfate Chemical compound CCCCCCCCCCCCOS(O)(=O)=O MOTZDAYCYVMXPC-UHFFFAOYSA-N 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- VLKZOEOYAKHREP-UHFFFAOYSA-N methyl pentane Natural products CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 239000000088 plastic resin Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Conductive Materials (AREA)
Description
【発明の詳細な説明】
本発明は、電極、導電体用に好適の高強度プラスチック
成形品の製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a high-strength plastic molded product suitable for electrodes and conductors.
すなわち、本発明は、膨張化黒鉛粉末及び黒鉛粉末をそ
れぞれ特殊な疎水化処理、すなわち、樹脂との、いわゆ
る1ぬれョをよくすることにより、樹脂と、膨張化黒鉛
粉末及び黒鉛粉末との、さらには界面活性剤との、混和
均質性を非常に高めた複合粉末、又は混練混合物を圧縮
成形機、押出成形機等の成形機及ひ成形型を用いて成形
することにより黒鉛の特性を十分に有し、特に非常に強
度に優れた電極、導電体用に好適のプラスチック成形品
を製造する方法に関するものである。近年、各種熱可塑
性樹脂にカーボンブラックや黒鉛粉末を添加し、混合後
、成形し、黒鉛の特性を有する黒鉛含有プラスチック成
形品が製造されている。That is, in the present invention, the expanded graphite powder and the graphite powder are subjected to a special hydrophobizing treatment, that is, to improve so-called 1-wetting with the resin, so that the relationship between the resin and the expanded graphite powder and the graphite powder is Furthermore, by molding a composite powder or kneaded mixture with a surfactant with extremely high mixing homogeneity using a molding machine such as a compression molding machine or an extrusion molding machine, or a molding mold, the characteristics of graphite can be sufficiently improved. The present invention relates to a method for manufacturing plastic molded products suitable for use in electrodes and conductors, particularly those having extremely high strength. In recent years, graphite-containing plastic molded products having the characteristics of graphite have been manufactured by adding carbon black or graphite powder to various thermoplastic resins, mixing them, and then molding them.
しかるに従来の黒鉛含有プラスチック成形品の製造方法
は、単に黒鉛粉末と熱可塑性樹脂粉末とをV型ミキサー
、ヘンシエル混合機等にて混合し、この混合粉末を圧縮
成形機、押出成形機等の成形機を用いて成形加工を行な
つている。この場合、黒鉛やカーボンブラックと熱可塑
性樹脂粉末との形状、粒度、比重や界面特性等が異なる
ため、均一な混合粉末が得られにくく、しかも熱可塑性
樹脂とのいわゆる1ぬれョが悪いため、したがつて圧縮
成形機、押出成形機の加熱部分において溶融樹脂中のカ
ーボンブラックや黒鉛粉末の分散が不均一となり、この
ため成形品中のカーボンブラックや黒鉛粉末の分散も不
均一であり、物理的並びに機械的特性(強度)はもちろ
ん、その他の黒鉛の特性にも大きなバラツキがあり実用
性・に乏しい。一方、混合の均一性を高める目的で黒鉛
と熱可塑性樹脂とをロールミキシング法、パンバリーミ
キシング法等の溶融混和法が考えられている。However, the conventional manufacturing method for graphite-containing plastic molded products is to simply mix graphite powder and thermoplastic resin powder in a V-type mixer, Henschel mixer, etc., and then mold this mixed powder in a compression molding machine, an extrusion molding machine, etc. The molding process is performed using a machine. In this case, because the graphite or carbon black and the thermoplastic resin powder have different shapes, particle sizes, specific gravity, interfacial properties, etc., it is difficult to obtain a uniform mixed powder, and furthermore, the so-called 1 wettability with the thermoplastic resin is poor. Therefore, the dispersion of carbon black and graphite powder in the molten resin becomes uneven in the heating section of the compression molding machine and extrusion molding machine, and therefore the dispersion of carbon black and graphite powder in the molded product is also uneven, resulting in physical problems. In addition to the mechanical properties (strength) and mechanical properties (strength), there are large variations in other properties of graphite, making it impractical. On the other hand, in order to improve the uniformity of mixing, methods of melt-blending graphite and thermoplastic resin, such as roll mixing and Panbury mixing, have been considered.
この方法は溶融混和した物を押出成形機等の成形機によ
り所望の形状に成形加工する方法である。しかし、この
方法は前述の方法による成形品に比べ、幾分均一な成形
品が得られるが、溶融混和時に黒鉛粉末の表面に吸着し
ている親水基等により熱可塑性樹脂との混和性、いわゆ
る1ぬれョが悪く、完全な黒鉛粉末の分散体が得られな
い。よつてこの混練混合物を用いて押出成形機等の成形
機により成形加工を行なつても、その成形品は黒鉛が均
一に分散されていないため、物理的並びに機械的特性(
強度)はもちろん、その他の黒鉛の特性にも大きなバラ
ツキがあり実用性に乏しい。又この方法においては、熱
可塑性樹脂との、いわゆる1ぬれョが悪いため多量の黒
鉛を添加することが困難となつている。さらに又、たと
えば均一なる混合が可能となつても、黒鉛の特性を十分
に引き出そうとすると添加する黒鉛量が多くなり、従つ
て脂肪分が減少するため、プラスチック成形品として必
要な強度が得られないのが現状である。This method is a method in which a melt-mixed product is molded into a desired shape using a molding machine such as an extruder. However, although this method yields a molded product that is somewhat more uniform than the molded product obtained by the above-mentioned method, the hydrophilic groups adsorbed on the surface of the graphite powder during melt-mixing make it difficult to mix with the thermoplastic resin. 1. Wetting is poor and a complete graphite powder dispersion cannot be obtained. Therefore, even if this kneaded mixture is molded using a molding machine such as an extrusion molding machine, the graphite is not uniformly dispersed in the molded product, resulting in poor physical and mechanical properties (
There are large variations not only in strength) but also in other properties of graphite, making it impractical. Furthermore, in this method, it is difficult to add a large amount of graphite due to poor wetting with the thermoplastic resin. Furthermore, even if homogeneous mixing becomes possible, in order to fully bring out the characteristics of graphite, the amount of graphite added will increase and the fat content will decrease, making it difficult to obtain the strength required for plastic molded products. The current situation is that there is no such thing.
すなわち、導電性や潤滑性等の黒鉛の特性を向上させよ
うとすれば強度が減少し、逆に強度を向上させようとす
れば黒鉛の特性が減少する。このため黒鉛含有プラスチ
ック成形品はその使用範囲が限定されており、今日、黒
鉛の特性を十分に有し、かつ非常に強い強度を有する、
例えば、電極、導電体用に好適の黒鉛含有プラスチック
成形品の出現が望まれる。本発明は以上の欠点を除去す
るためになされたもので、多量の黒鉛粉末の添加を可能
にし、かつ熱可塑性樹脂成形材料との親和性および混和
性、いわゆる1ぬれョを向上させることにより、均一な
溶融混合、並びに圧縮成形機、押出成形機の加熱部での
均一分散を可能にし、特に非常に強度に優れ十分な黒鉛
の特性を有し、かつバラツキの少ない均質な電極、導電
体用に好適のプラスチック成形品が得られる製造方法を
提供しようとするものである。That is, if an attempt is made to improve the properties of graphite such as conductivity or lubricity, the strength will decrease, and conversely, if an attempt is made to improve the strength, the properties of graphite will decrease. For this reason, the range of use of graphite-containing plastic molded products is limited, and today there are products that have all the characteristics of graphite and are extremely strong.
For example, the emergence of graphite-containing plastic molded products suitable for electrodes and conductors is desired. The present invention was made to eliminate the above-mentioned drawbacks, and by making it possible to add a large amount of graphite powder and improving the affinity and miscibility with thermoplastic resin molding materials, so-called 1 wettability, Enables uniform melt mixing and uniform dispersion in the heating section of compression molding machines and extrusion molding machines, especially for extremely strong and sufficient graphite properties, and homogeneous electrodes and conductors with little variation. The purpose of the present invention is to provide a manufacturing method that can produce plastic molded products suitable for.
本発明は先づ、嵩比重0.01〜0.033の繊維状膨
張黒鉛を粉砕するか又は、粉砕後、さらに造粒加工する
かして得られた粒径0.01〜1顛、嵩比重0.1〜0
.01の膨張化黒鉛粉末及び平均粒径0.1〜100μ
の黒鉛粉末を、それぞれ、(a)700を〜1100℃
の温度で真空高温加熱処理するか、(b)700を〜1
100℃の温度で水素ガス雰囲気高温加熱処理するか、
(c)700か〜1100℃の温度でメタンガス雰囲気
高温加熱処理するか、(d)n−ヘプタン、n−ブタン
、n−オクタン、ネオペンタン、3−メチルペンタン等
のアルカン族炭化水素により湿式処理を行なうか、又は
、(e)エチレン、プロピレン、ブチレン、1−ヘキセ
ン等のアルケン族炭化水素により湿式処理を行なうか、
して疎水化処理する工程(4)と、
(イ)疎水化処理した粒径0.01〜1TW11嵩比重
0.1〜0.01の膨張化黒鉛粉末3〜5踵量%と、(
口)疎水化処理した平均粒径0.1〜100μの黒鉛粉
末5〜90重量%と、(ハ)塩化ビニル樹脂、ポリエチ
レン樹脂、ポリプロピレン樹脂、ポリエステル樹脂、ポ
リウレタン樹脂、ポリアクリル樹脂、ポリメタクリル樹
脂、ポリアセタール樹脂、エチレン酢酸ビニル共重合体
樹脂、スチロール樹脂等の1種又は2種以上の熱可塑性
樹脂成形材料5〜9鍾量%と.を均一な複合粉末にする
混合、又は均一な混練混合にする混合工程(B)と、こ
の均一に混合させた複合粉末(イ+口+ハ)、又はこの
均一な混練混合物(イ+口+ハ)を圧縮成形機、押出成
形機等の成形機により所望の成形型により所望の形状に
成形加工する工程(C)との結合(A+B+C)からな
ることを特徴とする。The present invention first involves crushing fibrous expanded graphite having a bulk specific gravity of 0.01 to 0.033, or further granulating it after crushing. Specific gravity 0.1~0
.. 01 expanded graphite powder and average particle size 0.1-100μ
graphite powder at (a) 700 to 1100°C, respectively.
(b) 700 to 1
High-temperature heat treatment in a hydrogen gas atmosphere at a temperature of 100°C, or
(c) High-temperature heat treatment in a methane gas atmosphere at a temperature of 700 to 1100°C, or (d) Wet treatment with an alkane hydrocarbon such as n-heptane, n-butane, n-octane, neopentane, or 3-methylpentane. or (e) wet treatment with an alkene hydrocarbon such as ethylene, propylene, butylene, 1-hexene, etc.
step (4) of hydrophobizing the hydrophobized powder;
(1) 5 to 90% by weight of hydrophobized graphite powder with an average particle size of 0.1 to 100μ, and (c) vinyl chloride resin, polyethylene resin, polypropylene resin, polyester resin, polyurethane resin, polyacrylic resin, polymethacrylic resin. , polyacetal resin, ethylene-vinyl acetate copolymer resin, styrene resin, etc., or a thermoplastic resin molding material of 5 to 9% by weight. A mixing step (B) of mixing into a uniform composite powder or uniform kneading and mixing of this uniformly mixed composite powder (I + mouth + C) or this uniform kneading mixture (I + mouth + The method is characterized by combining (A+B+C) with step (C) of molding c) into a desired shape using a desired mold using a molding machine such as a compression molding machine or an extrusion molding machine.
又、本発明は先づ嵩比重0.01〜0.033の繊維状
膨張黒鉛を粉砕するか、又は粉砕後、さらに造粒加工す
るかして得られた粒径0.01〜1醜、嵩比重0.1〜
0.01の膨張化黒鉛粉末及び平均粒径0.1〜100
μの黒鉛粉末を、それぞれ、(a)7000〜1100
℃の温度で真空高温加熱処理するか、(b)7000〜
1100℃の温度で水素ガス雰囲気高温加熱処理するか
、(C)7000〜1100℃の温度でメタンガス雰囲
気高温加熱処理するか、(d)n−ヘプタン、n−ブタ
ン、n−オクタン、ネオペンタン、3−メチルペンタン
等のアルカン族炭化水素により湿式処理を行なうか、又
は、(e)エチレン、プロピレン、ブチレン、1−ヘキ
セン等のアルケン族炭化水素により湿式処理を行なうか
、して疎水化処理する工程(4)と、
(イ)疎水化処理した粒径0.01〜1wn1嵩比重0
.1〜0.01の膨張化黒鉛粉末3〜5鍾量%と、(口
)疎水化処理した平均粒径0.1〜100μの黒鉛粉末
5〜90重量%と、さらに、(ニ)ドデシル硫酸ナトリ
ウム、アルキルベンゼンスルホン酸ナトリウム、脂肪族
石けん樹脂酸石けん等の界面活性剤1〜5重量%と、(
ハ)塩化ビニル樹脂、ポリエチレン樹脂、ポリプロピレ
ン樹脂、ポリエステル樹脂、ポリウレタン樹脂、ポリア
クリル樹脂、ポリメタクリル樹脂、ポリアセタール樹脂
、エチレン酢酸ビニル共重合体樹脂、スチロール樹脂等
の1種又は2種以上の熱可塑性樹脂成形材料5〜9唾量
%とを均一な複合粉末にする混合、又は均一な混練混合
にする混合工程(B)″と、この均一に混合させた複合
粉末(イ+口+ハ+ニ)又は、この均一な混練混合物(
イ+口+ハ+ニ)を圧縮成形機、押出成形機等の成形機
により所望の成形型により所望の形状に成形加工する工
程(C)との結合(A+B″+C)からなることを特徴
とする。In addition, the present invention first crushes fibrous expanded graphite having a bulk specific gravity of 0.01 to 0.033, or after crushing, further granulates the particles with a particle size of 0.01 to 1. Bulk specific gravity 0.1~
0.01 expanded graphite powder and average particle size 0.1-100
(a) 7000 to 1100 μ graphite powder, respectively.
Vacuum high temperature heat treatment at a temperature of ℃ or (b) 7000~
(C) High temperature heat treatment in a methane gas atmosphere at a temperature of 7000 to 1100 °C; (d) n-heptane, n-butane, n-octane, neopentane, 3 - A step of hydrophobizing by performing a wet treatment with an alkane group hydrocarbon such as methylpentane, or (e) performing a wet treatment with an alkene group hydrocarbon such as ethylene, propylene, butylene, 1-hexene, etc. (4) and (a) Hydrophobized particle size 0.01-1wn1 bulk specific gravity 0
.. 1 to 0.01% by weight of expanded graphite powder, (1) 5 to 90% by weight of hydrophobized graphite powder with an average particle size of 0.1 to 100μ, and (d) dodecyl sulfuric acid. 1 to 5% by weight of a surfactant such as sodium, sodium alkylbenzene sulfonate, aliphatic soap resin acid soap, and (
c) One or more thermoplastics such as vinyl chloride resin, polyethylene resin, polypropylene resin, polyester resin, polyurethane resin, polyacrylic resin, polymethacrylic resin, polyacetal resin, ethylene vinyl acetate copolymer resin, styrene resin, etc. Mixing step (B)'' of mixing 5 to 9% resin molding material into a uniform composite powder, or uniform kneading, and the uniformly mixed composite powder (A+C+C+N). ) or this homogeneous kneaded mixture (
It is characterized by a combination (A+B''+C) with a step (C) of molding the A+C+C+D into a desired shape using a desired mold using a molding machine such as a compression molding machine or an extrusion molding machine. shall be.
すなわち、本発明においては、先づ前述のように、それ
ぞれ疎水化処理(A工程)した粒径0.01〜1Tmt
1嵩比重0.1〜0.01の膨張化黒鉛粉末及び平均粒
径0.1〜100pの黒鉛粉末をそれぞれ準備する。That is, in the present invention, first, as described above, particles having a particle size of 0.01 to 1 Tmt that have been subjected to hydrophobization treatment (Step A) are used.
1 Expanded graphite powder with a bulk specific gravity of 0.1 to 0.01 and graphite powder with an average particle size of 0.1 to 100p are respectively prepared.
しかして、この疎水化処理としては粉末に水素が吸着し
た場合、疎水性を示し、酸素が吸着した場合、親水性を
示すことに注目し、本発明においては、膨張化黒鉛粉末
及び黒鉛粉末を前述のように、700〜1100℃の温
度での真空加熱処理、700〜1100℃の温度での水
素ガス雰囲気加熱およびメタンガス雰囲気加熱による還
元処理、又は、疎水性官能基を有すると考えられるn−
ブタン、n−ヘプタン、n−オクタン、ネオペンタン、
3−メチルペンタン等のアルカン族炭化水素、又はエチ
レン、プロピレン、ブチレン、1−ヘキセン等のアルケ
ン族炭化水素による湿式処理を行なう。この疎水化処理
、すなわち、熱可塑性樹脂との均質混和性、いわゆる1
ぬれョの向上は、ロールミキシング法、パンバリーミキ
シング法、ヘンシエルミキシング法等の溶融混和法にお
いて極めて容易に均質混和が得られ、これにより多量の
膨張化黒鉛粉末及び黒鉛粉末の添加を可能にし、かつ熱
可塑性樹脂成形材料との完全な均一分散を可能にするた
めである。又、圧縮成形機、押出成形機等の成形機の加
熱部での熱可塑性樹脂との溶融液における完全な均一分
散を可能にするためてある。次に、膨張化黒鉛粉末の嵩
比重の限定、すなわち、0.1〜0.01としたのは、
0.1を越えると、黒鉛粉末及び熱可塑性樹脂との、い
わゆる、からみが弱くなり、成形後の物理的機械的強度
か向上せず、0.01未満の場合は、粉末の流動性およ
び混和性、すなわち、均一性が悪くなり偏析が顕著とな
り共に不可である。次に黒鉛粉末の粒度限定、すなわち
、0.1〜100μとしたのは、0.1μ未満の場合は
、通常工業的に入手が困難であり、コストも高くなり不
可である。However, in this hydrophobization treatment, it is noted that when hydrogen is adsorbed to the powder, the powder shows hydrophobicity, and when oxygen is adsorbed, it shows hydrophilicity, and in the present invention, expanded graphite powder and graphite powder are As mentioned above, vacuum heat treatment at a temperature of 700 to 1100°C, reduction treatment by heating in a hydrogen gas atmosphere and methane gas atmosphere heating at a temperature of 700 to 1100°C, or n-
Butane, n-heptane, n-octane, neopentane,
Wet treatment is performed using an alkane group hydrocarbon such as 3-methylpentane or an alkene group hydrocarbon such as ethylene, propylene, butylene, 1-hexene. This hydrophobization treatment, that is, homogeneous miscibility with thermoplastic resin, so-called 1
In order to improve wetting, homogeneous mixing can be obtained extremely easily in melt mixing methods such as roll mixing, Panbury mixing, and Henschel mixing, which makes it possible to add a large amount of expanded graphite powder and graphite powder. , and to enable complete uniform dispersion with the thermoplastic resin molding material. Further, it is intended to enable complete uniform dispersion of the thermoplastic resin in the melt in the heating section of a molding machine such as a compression molding machine or an extrusion molding machine. Next, the bulk specific gravity of the expanded graphite powder was limited to 0.1 to 0.01 because
If it exceeds 0.1, the so-called entanglement between graphite powder and thermoplastic resin will become weak, and the physical and mechanical strength after molding will not improve, and if it is less than 0.01, the fluidity and miscibility of the powder will deteriorate. In other words, the uniformity deteriorates and segregation becomes significant, making both of them unacceptable. Next, the particle size of the graphite powder is limited to 0.1 to 100 .mu.m. If it is less than 0.1 .mu.m, it is usually difficult to obtain it industrially and the cost becomes high.
又100μを越えると熱可塑性樹脂材料の種類によつて
は成形品の物理的機械的強度が低下するので不可てある
。次に、準備した(イ)疎水化処理した粒径0.01〜
1顛、嵩比重0.1〜0.01の膨張化黒鉛粉末3〜5
0重量%と、(口)疎水化処理した平均粒径0.1〜1
00μの黒鉛粉末5〜9鍾量%と、(ハ)塩化ビニル樹
脂、ポリエチレン樹脂、ポリプロピレン樹脂、ポリエス
テル樹脂、ポリウレタン樹脂、ポリアクリル樹脂、ポリ
メタクリル樹脂、ポリアセタール樹脂、エチレン酢酸ビ
ニル共重合体樹脂、スチロール樹脂等の1種又は2種以
上の熱可塑性樹脂成形材料5〜9鍾量%との均一な複合
粉末又は均一な混練混合物を得る。Moreover, if it exceeds 100 μm, the physical and mechanical strength of the molded product may decrease depending on the type of thermoplastic resin material, so it is not allowed. Next, prepared (a) hydrophobized particle size 0.01~
1 day, expanded graphite powder with bulk specific gravity 0.1-0.01 3-5
0% by weight and (mouth) hydrophobized average particle size 0.1-1
00 μ graphite powder 5 to 9 weight percent, (c) vinyl chloride resin, polyethylene resin, polypropylene resin, polyester resin, polyurethane resin, polyacrylic resin, polymethacrylic resin, polyacetal resin, ethylene vinyl acetate copolymer resin, A uniform composite powder or a uniform kneaded mixture with 5 to 9 weight percent of one or more thermoplastic resin molding materials such as styrene resin is obtained.
しかして、前記(イ)膨張化黒鉛粉末の数量限定、すな
わち、3〜5踵量%としたのは、3重量%未満の場合、
成形品において物理的機械的強度が向上せず、5唾量%
を越えるとコストが高くなるばかりか、黒鉛粉末自体の
特性に悪影響をおよぼすため共に不可である。Therefore, the reason for limiting the quantity of the expanded graphite powder (i), that is, 3 to 5% by weight, is that if the amount is less than 3% by weight,
The physical and mechanical strength of the molded product does not improve, and the amount of saliva is 5%.
Exceeding this value not only increases cost but also adversely affects the properties of the graphite powder itself, so both are unacceptable.
次に、前記(口)黒鉛粉末の数量限定、すなわち、5〜
9唾量%としたのは、5重量%未満では黒鉛粉末自体の
特性、すなわち、導電性、潤滑性が十分に出ず、9唾量
%を越えると、成形品において物理的機械的強度が減少
するため共に不可である。Next, limit the quantity of the graphite powder, that is, 5 to
The reason for setting the amount of saliva at 9% is that if it is less than 5% by weight, the properties of the graphite powder itself, such as conductivity and lubricity, will not be sufficiently exhibited, and if the amount exceeds 9%, the physical and mechanical strength of the molded product will deteriorate. Both are not possible because they decrease.
次に、前記(ハ)熱可塑性樹脂成形材料の数量限定、す
なわち、5〜9鍾量%としたのは、5重量%未満では成
形品において物理的機械的強度が得られず、90重量%
を越えると、黒鉛粉末の特性、すなわち、導電性、潤滑
性が得られず共に不可である。Next, the reason why the quantity of the thermoplastic resin molding material (c) was limited, that is, from 5 to 9% by weight, was because if it was less than 5% by weight, physical and mechanical strength could not be obtained in the molded product.
If it exceeds the above range, the characteristics of graphite powder, namely conductivity and lubricity, cannot be obtained, and both are unsuitable.
次に、熱可塑性樹脂成形材料としては、塩化ビニル樹脂
は、例えば、日本ゼオン株式会社製商品名ゼオン121
等、ポリエチレン樹脂は、例えば、製鉄化学株式会社製
商晶名フローセン、フローバック等、ポリプロピレン樹
脂は、例えば、三井東圧化学株式会社製商品名三井ノー
ブレンJ一700..JH−G等、ポリエステル樹脂は
、例えば、東洋紡績株式会社製商品名バイロン200,
30蒔、ポリウレタン樹脂は、例えば、日本ポリウレタ
ン株式会社製商品名バラプレン22S,25S等、ポリ
アクリル樹脂は、例えば、三菱レイヨン株式会社“製商
品名アクリペツト、アクリコン等、ポリアセタール樹脂
は、例えば、ポリプラスチック株式会社製商品名ジユラ
コンM−90,M−270等、スチロール樹脂は、例え
ば、三井東圧化学株式会社製商品名トーポレツクス85
0等、エチレン酢酸ビニル共重合体樹脂は、例えば、東
洋曹達工業株式会社製商品名ウルトラセン等、スチロー
ル樹脂は例えば、三井東圧化学株式会社製商品名トーポ
レツクス等を用いることができる。Next, as a thermoplastic resin molding material, vinyl chloride resin is used, for example, Zeon 121 (trade name) manufactured by Nippon Zeon Co., Ltd.
Examples of polyethylene resins include, for example, commercial names such as Flocene and Flowback, manufactured by Seitetsu Kagaku Co., Ltd., and polypropylene resins, such as Mitsui Noblen J-700, manufactured by Mitsui Toatsu Chemical Co., Ltd. .. Examples of polyester resins such as JH-G include Vylon 200 (trade name) manufactured by Toyobo Co., Ltd.
Polyurethane resins include, for example, Baraprene 22S and 25S manufactured by Nippon Polyurethane Co., Ltd.; polyacrylic resins include, for example, Acrypet and Acrycon manufactured by Mitsubishi Rayon Co., Ltd., and polyacetal resins include, for example, polyplastics. Styrene resins such as Giuracon M-90, M-270, manufactured by Mitsui Toatsu Chemical Co., Ltd., are available under the trade name Toporex 85, manufactured by Mitsui Toatsu Chemical Co., Ltd.
Ethylene-vinyl acetate copolymer resins such as 0, etc. can be used, for example, such as Ultracene (trade name, manufactured by Toyo Soda Kogyo Co., Ltd.), and styrene resins, such as Topolex (trade name, manufactured by Mitsui Toatsu Chemical Co., Ltd.) can be used.
又、本発明においては、前記(イ)疎水化処理した膨張
化黒鉛粉末3〜5鍾量%と、前記(ロ)疎水化処理した
黒鉛粉末5〜9鍾量%と、前記(ハ)熱可塑性樹脂5〜
9鍾量%と、さらに(ニ)ドデシル硫酸ナトリウム、ア
ルキルベンゼンスルホン酸ナトリウム、脂肪族石けん、
樹脂酸石けん等の界面活性剤1〜5重量%との均一な複
合粉末又は均一な混練混合物を得る。In addition, in the present invention, the above-mentioned (a) 3 to 5 weight percent of the expanded graphite powder subjected to the hydrophobization treatment, the above-mentioned (b) 5 to 9 weight percent of the graphite powder subjected to the hydrophobization treatment, and the above-mentioned (c) heat Plastic resin 5~
9 weight%, and (d) sodium dodecyl sulfate, sodium alkylbenzene sulfonate, aliphatic soap,
A homogeneous composite powder or a homogeneous kneaded mixture with 1 to 5% by weight of a surfactant such as a resin acid soap is obtained.
しかして、前記(ニ)界面活性剤の数量限定、すなわち
、1〜5重量%としたのは、1重量%未満では、ロール
ミキシング法、パンバリーミキシング法等の溶融混合に
おいて膨張化黒鉛粉末及び黒鉛粉末と熱可塑性樹脂成形
材料との、いわゆる1ぬれョを助けて、速やかに均一分
散させることができす、又、圧縮成形機、押出成形機等
の成形機の加熱部での膨張化黒鉛粉末及び黒鉛粉末と熱
可塑性樹脂成形材料との、いわゆる1ぬれョを助けて速
やかに均一分散させることができず、不可である。Therefore, the reason for limiting the amount of surfactant (d), that is, 1 to 5% by weight, is that if it is less than 1% by weight, expanded graphite powder and By helping the so-called 1-wetting of graphite powder and thermoplastic resin molding material, it is possible to quickly and uniformly disperse graphite powder and thermoplastic resin molding material.Also, expanded graphite can be used in the heating section of molding machines such as compression molding machines and extrusion molding machines. It is impossible to quickly and uniformly disperse the powder or graphite powder and the thermoplastic resin molding material by promoting so-called one-wetting.
5重量%を越えると、黒鉛の特性、すなわち導電性、潤
滑性及び成形品としての物理的機械的強度が減少する傾
向となり不可である。If it exceeds 5% by weight, the properties of graphite, ie, electrical conductivity, lubricity, and physical and mechanical strength as molded products tend to decrease, and this is not acceptable.
次に、混合方法としては、熱可塑性樹脂成形材料が、粉
末の場合、ロールミキシング法、パンバリーミキシング
法、ヘンシエルミキシング法、ボールミルミキシング法
等を用いることができる。Next, as a mixing method, when the thermoplastic resin molding material is a powder, roll mixing method, Panbury mixing method, Henschel mixing method, ball mill mixing method, etc. can be used.
又、熱可塑性樹脂成形材料がペレット状又はチップ状の
場合は、ロールミキシング法、パンバリーミキシング法
等にて混合できる。次に本発明においては、以上により
得られた均一なる複合粉末又は混練混合物を用い、圧縮
成形機、押出成形機等の成形機を用い、所望の成形型に
て所望する形状に成形加工する。Furthermore, when the thermoplastic resin molding material is in the form of pellets or chips, it can be mixed by a roll mixing method, a Panbury mixing method, or the like. Next, in the present invention, the uniform composite powder or kneaded mixture obtained as described above is molded into a desired shape in a desired mold using a molding machine such as a compression molding machine or an extrusion molding machine.
なお、成形条件は、通常の樹脂成形の場合と同じであり
、例えば、押出成形においては、熱可塑性樹脂の種類に
より多少は異なるが、次の通りである。The molding conditions are the same as those for ordinary resin molding, and for example, in extrusion molding, the conditions are as follows, although they differ somewhat depending on the type of thermoplastic resin.
スクリュー回転10〜80r.p.m.、加熱部温度7
0〜310℃。Screw rotation 10-80r. p. m. , heating section temperature 7
0-310℃.
又、成形機としては圧縮成形機、押出成形機、射出成形
機、吹込成形機等を用いることもできる。Further, as the molding machine, a compression molding machine, an extrusion molding machine, an injection molding machine, a blow molding machine, etc. can also be used.
本発明によるプラスチック成形品は、黒鉛の特性、すな
わち、導電性、潤滑性を十分に有し、かつ膨張化黒鉛粉
末と黒鉛粉末及び熱可塑性樹脂成形材料とのいわゆるか
らみのため非常に物理的機械的強度に優れており、かつ
、そのバラツキが少ない。The plastic molded product according to the present invention has the characteristics of graphite, that is, sufficient electrical conductivity and lubricity, and because of the so-called entanglement of expanded graphite powder, graphite powder, and thermoplastic resin molding material, it is extremely difficult to use physical machinery. It has excellent mechanical strength and has little variation.
導電性が均一で良好であり、電極、導電体用に好適であ
る。例えば、又、従来のプラスチック軸受等は潤滑性、
耐摩耗性に劣り、黒鉛等の固体潤滑剤の添加が検討され
たが、添加することにより必要とする物理的機械的強度
が得られす、改善が要求されている。本発明により得た
軸受は潤滑性、耐摩耗性を十分に有し、その物理的強度
もプラスチック単体に比べて5〜10%減少するだけで
あり十分使用に耐え得る物理的強度を有する。又、本発
明によるプラスチック成形品は、黒鉛粉末のみ添加した
成形品に比べて物理的機械的強度が20〜80%向上し
た。しかも良好な導電性のため信頼性の高い電極や導電
体となる。さらに、これらの成形品を加熱して熱可塑性
樹脂を炭化した後も、その物理的機械的強度は、黒鉛粉
末のみ添加した物に比べて物理的強度は20〜80%の
向上が認められた。It has uniform and good electrical conductivity and is suitable for electrodes and conductors. For example, conventional plastic bearings have lubricity,
The abrasion resistance is poor, and the addition of solid lubricants such as graphite has been considered, but the required physical and mechanical strength cannot be obtained by adding solid lubricants, so improvements are required. The bearing obtained according to the present invention has sufficient lubricity and wear resistance, and its physical strength is only 5 to 10% lower than that of plastic alone, so it has sufficient physical strength to withstand use. Moreover, the plastic molded article according to the present invention has improved physical and mechanical strength by 20 to 80% compared to a molded article to which only graphite powder is added. Moreover, because of its good conductivity, it becomes a highly reliable electrode or conductor. Furthermore, even after these molded products were heated to carbonize the thermoplastic resin, their physical and mechanical strength was found to be improved by 20 to 80% compared to products with only graphite powder added. .
これも注目すべきことである。又、本発明の方法は、熱
硬化性樹脂にも適用できることは勿論である。This is also noteworthy. Furthermore, it goes without saying that the method of the present invention can also be applied to thermosetting resins.
以下実施例についてさらに説明する。Examples will be further described below.
実施例1
粒径0.10〜0.85wn、嵩比重0.05の膨張化
黒鉛粉末及び平均粒径10μの黒鉛粉末をそれぞれ、7
00℃の温度による真空加熱処理により疎水化を行なつ
た。Example 1 Expanded graphite powder with a particle size of 0.10 to 0.85wn and bulk specific gravity of 0.05 and graphite powder with an average particle size of 10μ were each
Hydrophobization was performed by vacuum heat treatment at a temperature of 00°C.
この(イ)疎水化処理した膨張化黒鉛粉末1鍾量%と、
(口)同じく疎水化処理した黒鉛粉末7呼量%と、(ハ
)塩化ビニル樹脂成形材料田本ゼオン株式会社製商品名
ゼオン121)2唾量%とをホツトロールミキシツグに
て均一に溶融混和(イ+口+ハ)後、射出成形機又は、
圧縮成形機により成形加工して導電板を得た。この導電
板の強度は従来品に比べて65〜75%向上していた。
勿論導電性も”十分であつて、電極にも好適であつた。
なお、前記の膨張化黒鉛粉末を使用しないもの、及び前
記の疎水化処理を行なわなかつたものは、機械的強度弱
く、又導電性のバラツキも大きく、その値も低下したも
のになり、電極には使えなかつた。実施例2粒径0.1
9〜0.95T!r!n1嵩比重0.02の膨張化黒鉛
粉末と平均粒径7μの黒鉛粉末とをそれぞれ800℃の
温度による水素ガス雰囲気により疎水化を行なつた。This (a) 1 weight% of hydrophobized expanded graphite powder,
(1) 7% by weight of graphite powder, which has also been subjected to hydrophobization treatment, and (3) 2% by weight (trade name: Zeon 121), a vinyl chloride resin molding material manufactured by Tamoto Zeon Co., Ltd., are uniformly melted in a hot roll mixer. After mixing (I + mouth + C), injection molding machine or
A conductive plate was obtained by molding using a compression molding machine. The strength of this conductive plate was improved by 65 to 75% compared to conventional products.
Of course, the conductivity was also sufficient and suitable for electrodes.
In addition, those that do not use the above-mentioned expanded graphite powder and those that do not undergo the above-mentioned hydrophobization treatment have weak mechanical strength, large variations in conductivity, and a decrease in the value. could not be used. Example 2 Particle size 0.1
9~0.95T! r! Expanded graphite powder with an n1 bulk specific gravity of 0.02 and graphite powder with an average particle size of 7 μm were each hydrophobized in a hydrogen gas atmosphere at a temperature of 800°C.
この(イ)疎水化処理した膨張化黒鉛粉末2鍾j量%と
、(口)同じく疎水化処理した黒鉛粉末6踵量%と、(
ハ)ポリエチレン樹脂成形材料(製鉄化学株式会社製商
品名フローセンUF−7)20重量%とを、ヘンシエル
ミキシング法にて均一に混合(イ+口+ハ)し、圧縮成
形機により成形加工して導電板を得た。この導電板の強
度は従来品に比べて70〜80%向上していた。勿論導
電性も十分であつた。なお、前記の疎水化処理を省略し
た場合には導電性が低く、かつそのバラツキが見られ、
機械的強度も低かつた。実施例3
粒径0.20〜0.80Tf0n1嵩比重0.08の膨
張化黒鉛粉末と、平均粒径3μの黒鉛粉末とをそれぞれ
700℃の温度によるメタンガス雰囲気により疎水化を
行なつた。This (a) 2% amount of expanded graphite powder that has been subjected to hydrophobization treatment, (2) 6% amount of graphite powder that has also been subjected to hydrophobization treatment, and (
c) 20% by weight of a polyethylene resin molding material (trade name: Flocene UF-7, manufactured by Seitetsu Kagaku Co., Ltd.) was mixed uniformly using the Henschel mixing method (a + mouth + c), and molded using a compression molding machine. A conductive plate was obtained. The strength of this conductive plate was improved by 70 to 80% compared to conventional products. Of course, the conductivity was also sufficient. In addition, when the above-mentioned hydrophobization treatment is omitted, the conductivity is low and its dispersion is observed.
Mechanical strength was also low. Example 3 Expanded graphite powder with a particle size of 0.20 to 0.80Tf0n1 and bulk specific gravity of 0.08 and graphite powder with an average particle size of 3μ were each hydrophobized in a methane gas atmosphere at a temperature of 700°C.
この(イ)疎水化処理した膨張化黒鉛粉末8重量%と、
(口)同じく疎水化処理した黒鉛粉末22重量%と、(
ハ)ポリプロピレン樹脂成形材料(三井東圧化学株式会
社製商品名三井ノーブレンJ一700)6唾量%とを、
ホットロールミキシングにて均一に溶融混和(イ+口+
ハ)後、射出成形機、又は押出成形機により成形加工し
て軸受、ブッシングを得た。この軸受ブッシングの強度
は従来品に比べて70〜80%向上していた。勿論潤滑
性、耐摩耗性も十分であつた。このものも電極、導電体
用に好適であつた。機械的強度大にして導電性も高く、
かつバラツキが少なく信頼性の大きいものであつた。実
施例4
粒径0.20−0.80Twt1嵩比重0.03の膨張
化黒鉛粉末と、平均粒径3μの黒鉛粉末とをそれぞれn
−ブタンによる湿式処理を行ない、加熱乾燥によつて疎
水化を共に行なつた。This (a) 8% by weight of expanded graphite powder subjected to hydrophobization treatment,
(mouth) 22% by weight of graphite powder that was also hydrophobized and (
c) Polypropylene resin molding material (trade name Mitsui Noblen J-700 manufactured by Mitsui Toatsu Chemical Co., Ltd.) with 6% saliva content,
Melt and mix uniformly using hot roll mixing (I + mouth +
c) After that, it was molded using an injection molding machine or an extrusion molding machine to obtain a bearing and a bushing. The strength of this bearing bushing was improved by 70 to 80% compared to conventional products. Of course, the lubricity and wear resistance were also sufficient. This product was also suitable for electrodes and conductors. It has high mechanical strength and high conductivity.
Moreover, it was highly reliable with little variation. Example 4 Expanded graphite powder with a particle size of 0.20-0.80Twt1 and bulk specific gravity of 0.03 and graphite powder with an average particle size of 3μ were each
- Wet treatment with butane was carried out, and hydrophobization was also carried out by heating and drying.
この(イ)疎水化処理した膨張化黒鉛粉末3重量%と、
(口)同じく疎水化処理した黒鉛粉末25重量%と、(
ハ)ポリアセタール樹脂成形材料(ポリプラスチック株
式会社製商品名ジユラコンM−270)7鍾量%とを、
ホットロールミキシングにて均一に溶融混和(イ+口+
ハ)後、射出成形機により成形加工して、軸受、ブッシ
ングを得た。この軸受、ブッシングの強度は従来品に比
べて65〜75%向上していた。勿論潤滑.性、耐摩耗
性も十分であつた。勿論、電極、導電体用として好適で
あつた。機械的強度大にして、実用上、信頼性があつた
。実施例5
粒径0.05〜0.4『、嵩比重0.03の膨張化黒鉛
粉・末と、平均粒径80μの黒鉛粉末とを、それぞれ8
00℃の温度による真空加熱処理により疎水化を行なつ
た。This (a) 3% by weight of expanded graphite powder subjected to hydrophobization treatment,
(mouth) 25% by weight of graphite powder that was also hydrophobized and (
C) polyacetal resin molding material (product name: Jyuracon M-270 manufactured by Polyplastics Co., Ltd.) with a weight of 7%,
Melt and mix uniformly using hot roll mixing (I + mouth +
c) After that, it was molded using an injection molding machine to obtain a bearing and a bushing. The strength of this bearing and bushing was improved by 65 to 75% compared to conventional products. Of course, lubrication. It also had sufficient strength and abrasion resistance. Of course, it was suitable for electrodes and conductors. It has high mechanical strength and is reliable in practical use. Example 5 Expanded graphite powder/powder with a particle size of 0.05 to 0.4'', bulk specific gravity of 0.03, and graphite powder with an average particle size of 80 μm were each
Hydrophobization was performed by vacuum heat treatment at a temperature of 00°C.
この(イ)疎水化処理した膨張化黒鉛粉末1種量%と、
(口)同じく疎水化処理した黒鉛粉末60重量%と、(
ハ)ポリアクリル樹脂成形材料(三菱レーヨン株式会社
製商品名アクリコン)20重量%と、(ニ)ドデシル硫
酸ナトリウム3重量%とを、ヘンシエルミキシングにて
均一に混合(イ+口+ハ+ニ)後、圧縮成形機により成
形加工して導電板を得た。この導電板の強度は従来品に
比べて50〜60%向上していた。勿論導電性も十分で
あつた。電極、導電体用に好適であつた。実用上信頼性
大であつた。ノ実施例6
粒径0.34〜1.0−、嵩比重0.01の膨張化黒鉛
粉末と、平均粒径5μの黒鉛粉末とをそれぞれn−ヘプ
タンによる湿式処理を行ない、加熱乾燥によつて疎水化
を行なつた。This (a) 1% of hydrophobized expanded graphite powder,
(mouth) 60% by weight of graphite powder that was also hydrophobized and (
C) 20% by weight of a polyacrylic resin molding material (trade name: Acrycon, manufactured by Mitsubishi Rayon Co., Ltd.) and (d) 3% by weight of sodium dodecyl sulfate were uniformly mixed using Henschel mixing (A+B+C+N). ), and then molded using a compression molding machine to obtain a conductive plate. The strength of this conductive plate was improved by 50 to 60% compared to conventional products. Of course, the conductivity was also sufficient. It was suitable for electrodes and conductors. It was highly reliable in practice. Example 6 Expanded graphite powder with a particle size of 0.34 to 1.0- and bulk specific gravity of 0.01 and graphite powder with an average particle size of 5 μm were wet-treated with n-heptane and dried by heating. Then, we made it hydrophobic.
この(イ)疎水化処理した膨・張化黒鉛粉末1鍾量%と
、(口)同じく疎水化処理した黒鉛粉末6呼量%と、(
ハ)エチレン酢酸ビニル共重合体樹脂成形材料(東洋曹
達工業株式会社製商品名ウルトラセン)25重量%と、
(ニ)アルキルベンゼンスルホン酸ナトリウム5重量%
とを、ボール゛ミルミキシング法にて均一に混合(イ+
口+ハ+ニ)後、圧縮成形機により成形加工して導電板
を得た。この導電板の強度は従来品に比べて50〜60
%向上していた。勿論導電性も十分であつた。薄手の電
極、導電体用としても好適てあつた。又、この導電板を
加熱して樹脂を炭化した後もその強度は40〜50%向
上していた。実施例7
粒径0.05〜0.65Tm1嵩比重0.05の膨張化
黒鉛粉末と、平均粒径7μの黒鉛粉末とをそれぞれエチ
レンによる湿式処理を行ない減圧乾燥によつて疎水化を
行なつた。This (a) 1 weight% of expanded/expanded graphite powder that has been subjected to hydrophobization treatment, (1) 6 weight% of graphite powder that has also been subjected to hydrophobization treatment, (
C) 25% by weight of ethylene-vinyl acetate copolymer resin molding material (trade name: Ultrasen, manufactured by Toyo Soda Kogyo Co., Ltd.);
(d) Sodium alkylbenzenesulfonate 5% by weight
are mixed uniformly using the ball mill mixing method (I +
After that, it was molded using a compression molding machine to obtain a conductive plate. The strength of this conductive plate is 50 to 60 times stronger than conventional products.
% improved. Of course, the conductivity was also sufficient. It was also suitable for thin electrodes and conductors. Furthermore, even after the conductive plate was heated to carbonize the resin, its strength was improved by 40 to 50%. Example 7 Expanded graphite powder with a particle size of 0.05 to 0.65Tm1 and bulk specific gravity of 0.05 and graphite powder with an average particle size of 7μ were each subjected to wet treatment with ethylene and hydrophobized by drying under reduced pressure. Ta.
この(イ)疎水化処理した膨張化黒鉛粉末3重量%と、
(口)同じく疎水化処理した黒鉛粉末25重量%と、(
ハ)スチロール樹脂成形材料(三井東圧化学株式会社製
商品名トーポレツクス)70重量%と、(ニ)脂肪族石
けん2重量%とを、ホットロールミキシングにて均一に
溶融混和(イ+口+ハーニ)後、押出成形機、又は射出
成形機により成形加工して軸受を得た。この軸受の強度
は従来品に比べて65〜75%向上していた。勿論潤滑
性、耐摩耗性も十分であつた。勿論、このものは電極、
導電体用としても好適てあつた。導電性高く、かつバラ
ツキが少なく、機械的強度大で信頼性があつた。実施例
8
粒径0.05〜0.4−、嵩比重0.06の膨張化黒鉛
粉末と、平均粒径30μの黒鉛粉末とを、それぞれ70
0′Cの温度による水素ガス雰囲気により疎水化を行な
つた。This (a) 3% by weight of expanded graphite powder subjected to hydrophobization treatment,
(mouth) 25% by weight of graphite powder that was also hydrophobized and (
C) 70% by weight of a styrene resin molding material (trade name TOPOLEX, manufactured by Mitsui Toatsu Chemical Co., Ltd.) and (d) 2% by weight of aliphatic soap are uniformly melted and mixed using hot roll mixing. ), and then molded using an extrusion molding machine or an injection molding machine to obtain a bearing. The strength of this bearing was improved by 65 to 75% compared to conventional products. Of course, the lubricity and wear resistance were also sufficient. Of course, this thing is an electrode,
It was also suitable for use as a conductor. It had high conductivity, little variation, high mechanical strength, and was reliable. Example 8 Expanded graphite powder with a particle size of 0.05 to 0.4- and bulk specific gravity of 0.06 and graphite powder with an average particle size of 30μ were each
Hydrophobization was carried out in a hydrogen gas atmosphere at a temperature of 0'C.
この(イ)疎水化処理した膨張化黒鉛粉末9重量%と、
(口)同じく疎水化処理した黒鉛粉末68重量%と、(
ハ)フェノール樹脂成形材料(住友ベークライト株式会
社製商品名PR−11078)2鍾量%とを、ヘンジエ
ルミキシングにて均一に混合(イ+口+ハ)し、圧縮成
形機にて成形加工して導電板を得た。この導電板の強度
は従来品に比べて70〜80%向上していた。勿論、導
電性も十分であつた。薄手の電極にも好適であつた。本
発明に係る疎水化処理を施した黒鉛粉末と、疎水処理を
施さなかつた黒鉛粉末とでは、まず、ホットロールミキ
シング及びヘンシエルミキシングにおいて、均一に分散
させるのに要する時間が、未処理粉末を100とすると
、処理粉末は30〜50と112〜113の時間ですむ
。This (a) 9% by weight of expanded graphite powder subjected to hydrophobization treatment,
(mouth) 68% by weight of graphite powder that was also hydrophobized and (
C) Mix phenolic resin molding material (trade name PR-11078 manufactured by Sumitomo Bakelite Co., Ltd.) with a weight of 2% using Henjiel mixing (a + mouth + c), and mold it using a compression molding machine. A conductive plate was obtained. The strength of this conductive plate was improved by 70 to 80% compared to conventional products. Of course, the conductivity was also sufficient. It was also suitable for thin electrodes. First, in hot roll mixing and Henschel mixing, the time required to uniformly disperse the graphite powder that has been subjected to the hydrophobic treatment according to the present invention and the graphite powder that has not been subjected to the hydrophobic treatment is longer than that of the untreated powder. 100, the processed powder requires 30-50 and 112-113 hours.
又、前記各実施例における成形品の強度(曲げ強度)と
導電性とを挙げる。In addition, the strength (bending strength) and conductivity of the molded products in each of the above examples will be listed.
強度と導電性の比較Comparison of strength and conductivity
Claims (1)
膨張化黒鉛粉末及び平均粒径0.1〜100μの黒鉛粉
末をそれぞれ、(a)700°〜1100℃の温度で真
空高温加熱処理するか、(b)700°〜1100℃の
温度で水素ガス雰囲気高温加熱処理するか、(c)70
0°〜1100℃の温度でメタンガス雰囲気高温加熱処
理するか、(d)n−ブタン、n−ヘプタン、n−オク
タン、ネオペンタン、3−メチルペンタン等のアルカン
族炭化水素により湿式処理を行なうか、又は、(e)エ
チレン、プロピレン、ブチレン、1−ヘキセン等のアル
ケン族炭化水素により湿式処理を行なうか、して疎水化
処理する工程(A)と、 (イ)疎水化処理した粒径0.01〜1mm、嵩比重0
.1〜0.01の膨張化黒鉛粉末、3〜50重量%と、
(ロ)同じく疎水化処理した平均粒径0.1〜100μ
の黒鉛粉末5〜90重量%と、(ハ)塩化ビニル樹脂、
ポリエチレン樹脂、ポリプロピレン樹脂、ポリエステル
樹脂、ポリウレタン樹脂、ポリアクリル樹脂、ポリメタ
クリル樹脂、ポリアセタール樹脂、エチレン酢酸ビニル
共重合体樹脂、スチロール樹脂等の1種又は2種以上の
熱可塑性樹脂成形材料5〜90重量%とを均一な複合粉
末にする混合又は均一な混練混合にする混合工程(B)
と、この均一に混合させた複合粉末(イ+ロ+ハ)又は
この均一な混練混合物(イ+ロ+ハ)を圧縮成形機、押
出成形機等の成形機により所望の成形型により所望の形
状に成形加工する工程(C)との結合(A+B+C)か
らなることを特徴とする電極、導電体用に好適の高強度
プラスチック成形品の製造方法。 2 粒径0.01〜1mm、嵩比重0.1〜0.01の
膨張化黒鉛粉末及び平均粒径0.1〜100μの黒鉛粉
末をそれぞれ、(a)700°〜1100℃の温度で真
空高温加熱処理するか、(b)700°〜1100℃の
温度で水素ガス雰囲気高温加熱処理するか、(c)70
0°〜1100℃の温度でメタンガス雰囲気高温加熱処
理するか、(d)n−ブタン、n−ヘプタン、n−オク
タン、ネオペンタン、3−メチルペンタン等のアルカン
族炭化水素により湿式処理を行なうか、又は、(e)エ
チレン、プロピレン、ブチレン、1−ヘキセン等のアル
ケン族炭化水素により湿式処理を行なうか、して疎水化
処理する工程(A)と、 (イ)疎水化処理した粒径0.01〜1mm、嵩比重0
.1〜0.01の膨張化黒鉛粉末3〜50重量%と、(
ロ)同じく疎水化処理した平均粒径0.1〜100μの
黒鉛粉末5〜90重量%と、さらに(ニ)ドデシル硫酸
ナトリウム、アルキルベンゼンスルホン酸ナトリウム、
脂肪族石けん、樹脂酸石けん等の界面活性剤1〜5重量
%と、(ハ)塩化ビニル樹脂、ポリエチレン樹脂、ポリ
プロピレン樹脂、ポリエステル樹脂、ポリウレタン樹脂
、ポリアクリル樹脂、ポリメタクリル樹脂、ポリアセタ
ール樹脂、エチレン酢酸ビニル共重合体樹脂、スチロー
ル樹脂等の1種又は2種以上の熱可塑性樹脂成形材料5
〜90重量%とを均一な複合粉末にする混合、又は均一
な混練混合にする混合工程(B)′と、この均一に混合
させた複合粉末(イ+ロ+ハ+ニ)、又は、この均一な
混練混合物(イ+ロ+ハ+ニ)を圧縮成形機、押出成形
機等の成形機により所望の成形型により所望の形状に成
形加工する工程(C)との結合(A+B′+C)からな
ることを特徴とする電極、導電体用に好適の高強度プラ
スチック成形品の製造方法。[Scope of Claims] 1. Expanded graphite powder with a particle size of 0.01 to 1 mm and bulk specific gravity of 0.1 to 0.01, and graphite powder with an average particle size of 0.1 to 100μ, respectively, are heated at (a) 700° to (b) High temperature heat treatment in a hydrogen gas atmosphere at a temperature of 700° to 1100°C; (c) 70°C
High-temperature heat treatment in a methane gas atmosphere at a temperature of 0° to 1100°C, or (d) wet treatment with an alkane group hydrocarbon such as n-butane, n-heptane, n-octane, neopentane, 3-methylpentane, etc. or (e) step (A) of hydrophobizing by wet treatment with an alkene group hydrocarbon such as ethylene, propylene, butylene, 1-hexene, etc.; (a) the hydrophobized particles having a diameter of 0. 01~1mm, bulk specific gravity 0
.. 1 to 0.01 expanded graphite powder, 3 to 50% by weight,
(b) Average particle size 0.1 to 100 μm, which was also subjected to hydrophobization treatment
5 to 90% by weight of graphite powder, (c) vinyl chloride resin,
One or more thermoplastic resin molding materials such as polyethylene resin, polypropylene resin, polyester resin, polyurethane resin, polyacrylic resin, polymethacrylic resin, polyacetal resin, ethylene vinyl acetate copolymer resin, styrene resin, etc. 5 to 90 Mixing process (B) to make a uniform composite powder or to make a uniform kneading mixture with weight%
Then, this uniformly mixed composite powder (A + B + C) or this uniform kneaded mixture (A + B + C) is molded into a desired mold using a molding machine such as a compression molding machine or an extrusion molding machine. A method for manufacturing a high-strength plastic molded product suitable for electrodes and conductors, characterized by comprising a step (C) of forming into a shape and combining (A+B+C). 2. Expanded graphite powder with a particle size of 0.01 to 1 mm and bulk specific gravity of 0.1 to 0.01 and graphite powder with an average particle size of 0.1 to 100 μ, respectively, are (a) vacuum heated at a temperature of 700° to 1100°C. (b) High temperature heat treatment in a hydrogen gas atmosphere at a temperature of 700° to 1100°C; (c) 70°C
High-temperature heat treatment in a methane gas atmosphere at a temperature of 0° to 1100°C, or (d) wet treatment with an alkane group hydrocarbon such as n-butane, n-heptane, n-octane, neopentane, 3-methylpentane, etc. or (e) step (A) of hydrophobizing by wet treatment with an alkene group hydrocarbon such as ethylene, propylene, butylene, 1-hexene, etc.; (a) the hydrophobized particles having a diameter of 0. 01~1mm, bulk specific gravity 0
.. 3-50% by weight of expanded graphite powder of 1-0.01, (
b) 5 to 90% by weight of graphite powder with an average particle size of 0.1 to 100 μ which has also been subjected to hydrophobization treatment, and (d) sodium dodecyl sulfate, sodium alkylbenzene sulfonate,
1 to 5% by weight of a surfactant such as aliphatic soap or resin acid soap, and (c) vinyl chloride resin, polyethylene resin, polypropylene resin, polyester resin, polyurethane resin, polyacrylic resin, polymethacrylic resin, polyacetal resin, ethylene. One or more thermoplastic resin molding materials such as vinyl acetate copolymer resin, styrene resin, etc. 5
- 90% by weight into a uniform composite powder, or a mixing step (B)' where the mixture is uniformly kneaded, and this uniformly mixed composite powder (A + B + C + D), or this Combination with step (C) of molding the uniform kneaded mixture (A+B+C+D) into a desired shape using a desired mold using a molding machine such as a compression molding machine or an extrusion molding machine (A+B'+C) A method for producing a high-strength plastic molded product suitable for electrodes and conductors, characterized by comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56007144A JPS6054348B2 (en) | 1981-01-22 | 1981-01-22 | Method for manufacturing high-strength plastic molded products suitable for electrodes and conductors |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56007144A JPS6054348B2 (en) | 1981-01-22 | 1981-01-22 | Method for manufacturing high-strength plastic molded products suitable for electrodes and conductors |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57123858A JPS57123858A (en) | 1982-08-02 |
| JPS6054348B2 true JPS6054348B2 (en) | 1985-11-29 |
Family
ID=11657871
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56007144A Expired JPS6054348B2 (en) | 1981-01-22 | 1981-01-22 | Method for manufacturing high-strength plastic molded products suitable for electrodes and conductors |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6054348B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6031039A (en) * | 1996-09-18 | 2000-02-29 | E. I. Du Pont De Nemours And Company | Anti-static composition |
| JP2013516505A (en) * | 2009-12-31 | 2013-05-13 | エスゲーエル カーボン ソシエタス ヨーロピア | Graphite-containing plate and method for producing graphite-containing plate |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104302707B (en) | 2012-05-15 | 2018-08-28 | 日本瑞翁株式会社 | Conductive composition |
| JP6294123B2 (en) * | 2014-03-28 | 2018-03-14 | 出光ライオンコンポジット株式会社 | Resin composition and cleaning method using the same |
| GB2539862B (en) * | 2014-05-09 | 2021-03-03 | Council Scient Ind Res | An improved next generation off-laboratory polymer chip electrode |
-
1981
- 1981-01-22 JP JP56007144A patent/JPS6054348B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6031039A (en) * | 1996-09-18 | 2000-02-29 | E. I. Du Pont De Nemours And Company | Anti-static composition |
| JP2013516505A (en) * | 2009-12-31 | 2013-05-13 | エスゲーエル カーボン ソシエタス ヨーロピア | Graphite-containing plate and method for producing graphite-containing plate |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57123858A (en) | 1982-08-02 |
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