JPH0124724B2 - - Google Patents

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Publication number
JPH0124724B2
JPH0124724B2 JP59193263A JP19326384A JPH0124724B2 JP H0124724 B2 JPH0124724 B2 JP H0124724B2 JP 59193263 A JP59193263 A JP 59193263A JP 19326384 A JP19326384 A JP 19326384A JP H0124724 B2 JPH0124724 B2 JP H0124724B2
Authority
JP
Japan
Prior art keywords
particle size
average particle
kneaded
powder
weight
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
Application number
JP59193263A
Other languages
Japanese (ja)
Other versions
JPS6172610A (en
Inventor
Akio Kotado
Junichi Aizawa
Takeshi Ishikawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP59193263A priority Critical patent/JPS6172610A/en
Publication of JPS6172610A publication Critical patent/JPS6172610A/en
Publication of JPH0124724B2 publication Critical patent/JPH0124724B2/ja
Granted legal-status Critical Current

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  • Ceramic Products (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

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

(産業上の利用分野) 本発明は、高密度黒鉛材の製造法に関する。 (従来技術とその問題点) 高密度黒鉛材は、通常コークス粉、黒鉛粉、油
煙等の骨材にタールピツチ、コールタール、フエ
ノール樹脂等の結合材を加えて加熱混練した混練
物を押出し成形したり、混練物を粉砕し粒度調整
した成形粉を加圧成形、静水圧成形する等の手段
により所定の形状に成形して成形体を得、これを
マツフル炉、トンネル炉等の焼成炉において約
1000℃で焼成する。次いでこの焼成品をピツチ含
浸し再焼成する。このピツチ含浸、再焼成の工程
を必要回数行つた後、約3000℃の温度で黒鉛化す
る方法がとられている。このピツチ含浸作業は、
バツチ作業となることや含浸後の焼成品周囲のピ
ツチ除去に手間のかかること及び再焼成に長期の
工程が必要ないことなどから、この方法による高
密度黒鉛材は、コストが高く長期の時間がかかる
等の問題があつた。 そこで、最近仮焼コークスを原料としたHIP
(熱間静水圧プレス)による製造法、あるいはメ
ソカーボンマイクロビーズを使用する製造法が開
発された。しかし、HIPを使用する方法は高価な
装置を用いなければならないこと、又メソカーボ
ンマイクロビーズを用いる方法はこのマイクロビ
ーズの製造法が複雑な為に原料価格が高いこと及
び大型の製品の焼成がむずかしく不良率が高い等
の欠点があつた。 (発明の目的) 本発明は、上記した問題点を解決する高密度黒
鉛材の製造法を提供することを目的とする。 (発明の構成) 本発明は、骨材と結合材とを加熱混練し最大粒
径10μm以下に粗粉砕した混練物を300〜550℃の
温度で熱処理し、次いで平均粒径が骨材の平均粒
径の1.05倍以上で18μm以下に粉砕した後、成形、
焼成及び黒鉛化することを特徴とする高密度黒鉛
材の製造法に関する。 本発明における骨材とは、コークス粉、黒鉛
粉、油煙等の炭素材料粉体であり、結合材とはタ
ールピツチ、コールタールなどである。骨材の平
均粒径は15μm以下が好ましい。15μmを越える
と組織中の細孔径が大となり、高密度にするため
に不利になる。結合材は、固定炭素が35重量%以
上であることが好ましい。35重量%未満では、揮
発分の放出が多くなり高密度化のために不利にな
る。結合材の割合は、重量で25〜60%が好まし
い。25%未満では高密度化に充分でなく、60%を
越えると混練が不十分になり易い。 前記骨材及び結合材は、まずV型混合機等を用
いて充分に混合するか、混練時に充分に混合す
る。この混合物を双腕型〓和機、連続型〓和機等
を用いて混練するが、混練温度は混練物が最適粘
度になるように設定する。この混練温度は、特に
限定するものではないが、一般的には150〜300℃
である。 混練は、骨材と結合材が均一になり、結合材が
骨材をよくおおうように充分に行う。このように
して得られた混練物は塊状であるので、最大で10
mm以下の粒径に粗粉砕する必要がある。10mmを越
える混練物があると、熱処理で揮発分が抜けにく
く、内部と表面とで揮発分が均一に放出されない
からである。 このようにして得られた混練物を熱処理温度
300〜550℃で熱処理を行う。熱処理温度が300℃
未満では、揮発分の放出が長時間になり、一方
550℃を越えると混練物の焼結性がほとんどなく
なり目的の製品が得られない為である。熱処理は
酸化性雰囲気下でも可能であるが、処理温度が
350℃を超え、処理時間が40分以上になると酸化
が著しくなり物理特性が低下するので、非酸化性
雰囲気が好ましい。熱処理は好ましくは混練物の
揮発分が重量で5〜20%になるように行う。揮発
分が5%未満では黒鉛材の物理特性が充分でな
く、20%を越えるとふくれや亀裂が発生し易くな
る為である。 熱処理後の混練物は、粉砕機によつて粉砕す
る。粉砕機としては、ボールミル、振動ボールミ
ル、ジエツトミル、ターボミル、ピンミル等があ
るが特に限定するものではない。粉砕粉平均粒径
は、骨材粒子径の1.05倍以上で18μm以下が必要
である。1.05倍未満では、骨材表面の結合材量が
充分でなく結合力が低下し高密度材は得られな
い。また、この粉砕粉の平均粒径が18μmを越え
ると組織中の細孔径が大きくなり高密度材は得ら
れない。 この粉砕粉を加圧成形、静水圧成形等の公知の
手段により所定の形状に成形した成形体を得、こ
れをマツフル炉、トンネル炉などの焼成炉におい
て公知の方法で焼成し、更に2500℃以上の温度で
黒鉛化するが、これらの方法については特に限定
するものではない。 (実施例) 次に実施例を説明する。 実施例 1 平均粒径3μmのピツチコークス粉50重量部に、
平均粒径35μmに粉砕したタールピツチ粉50重量
部を加え、V型混合機により充分混合した。この
混合粉を双腕型〓和機により200℃の温度で加熱
しながら充分に混練し、冷却後最大粒径4mm以下
に粗粉砕した。これを窒素雰囲気中450℃で10分
間加熱して揮発分を14重量%とした。この混練物
を粗粉砕後、ボールミルで平均粒径が10μm粉に
なるまで粉砕を行い、加圧成形して得た成形体を
非酸化性雰囲気中約1000℃で焼成し、約3000℃で
黒鉛化した。この時の物理特性を第1表に示す。 実施例 2 平均粒径3μmのピツチコークス粉55重量部に
平均粒径35μmに粉砕したタールピツチ粉45重量
部を加え、V型混合機により充分混合した。この
混合粉を連続型〓和機により170℃の温度で加熱
しながら充分に混練し、冷却後最大粒径4mm以下
に粗粉砕を行つた。これを窒素雰囲気中400℃で
10分間加熱して揮発分を16重量%とした。この混
練物を粗粉砕後ジエツトミルで平均粒径が8μm
になるまで粉砕を行い、次に加圧成形して得た成
形体を非酸化性雰囲気中約1000℃で焼成し、約
3000℃で黒鉛化を行つた。この時の物理特性を第
1表に示す。 実施例 3 平均粒径20nmのカーボンブラツク45重量部に
平均粒径10μmに粉砕したタールピツチ粉55重量
部を加え、V型混合機により充分混合した。この
混合粉を双腕型〓和機により190℃の温度で加熱
しながら充分に混練し、冷却後粗粉砕を行い最大
粒径4mm以下の粗粒を得た。これを窒素雰囲気中
450℃で25分間加熱し揮発分を12重量%とした。
この混練物を振動ミルで平均粒径が6μmになる
まで粉砕を行い、この粉末を加圧成形して得た成
形体を非酸化性雰囲気中約1000℃で焼成し、約
3000℃で黒鉛化を行つた。この時の物理特性を第
1表に示す。 比較例 1 平均粒径25μmのピツチコークス粉65重量部
に、粉砕したタールピツチ粉35重量部を加え、V
型混合機により充分混合した。この混合粉を双腕
型〓和機により200℃の温度で加熱しながら3時
間混練を行つた。この混練物を粉砕し、平均粒径
35μmとした。揮発分は9%であり、実施例1と
同様に成形、焼成、黒鉛化を行つた。この物理特
性を第1表に示す。 比較例 1 比較例1で得た焼成体にピツチ含浸を行い、再
焼成後実施例1と同様にして黒鉛化を行つた。こ
れらの物理特性を第1表に示す。 実施例 4 平均粒径10μmのピツチコークス粉60重量部
に、平均粒径35μmに粉砕したタールピツチ粉40
重量部を加え混合機により充分混合した。この混
合粉を連続型〓和機により220℃の温度で加熱し
ながら充分に混練し冷却後粗粉砕して最大粒径4
mm以下の粗粒を得た。これを大気中350℃で25分
間加熱し揮発分を11重量%とした。この混練物を
振動ミルで平均粒径が12μmになるまで粉砕し、
粉砕粉を加圧成形後非酸化性雰囲気中約1000℃で
焼成し、約3000℃の温度で黒鉛化を行つた。この
時の物理特性の値を第1表に示す。
(Industrial Application Field) The present invention relates to a method for producing high-density graphite material. (Prior art and its problems) High-density graphite materials are usually made by extrusion molding a mixture obtained by heating and kneading aggregates such as coke powder, graphite powder, and oil smoke with the addition of binders such as tar pitch, coal tar, and phenolic resin. Alternatively, the kneaded material is pulverized, the particle size is adjusted, and the molded powder is molded into a predetermined shape by means such as pressure molding or isostatic pressing to obtain a molded product, which is then heated in a firing furnace such as a Matsufuru furnace or a tunnel furnace.
Fire at 1000℃. This fired product is then impregnated with pitch and fired again. After performing this pitch impregnation and re-firing process a necessary number of times, a method is used in which the material is graphitized at a temperature of about 3000°C. This pitch impregnation work is
This method is expensive and takes a long time to produce high-density graphite material because it requires batch work, it is time-consuming to remove the pitch around the fired product after impregnation, and there is no need for a long process for re-firing. There were such problems. Therefore, recently HIP using calcined coke as raw material has been developed.
A manufacturing method using hot isostatic pressing (hot isostatic pressing) or using mesocarbon microbeads has been developed. However, the method using HIP requires the use of expensive equipment, and the method using mesocarbon microbeads requires high raw material costs due to the complicated manufacturing method of the microbeads, and requires the firing of large products. It had drawbacks such as being difficult and having a high defective rate. (Object of the Invention) An object of the present invention is to provide a method for producing a high-density graphite material that solves the above-mentioned problems. (Structure of the Invention) The present invention heat-treats a kneaded material obtained by heating and kneading aggregate and a binder and coarsely pulverizing the material to a maximum particle size of 10 μm or less at a temperature of 300 to 550°C, and then After pulverizing to 18 μm or more at least 1.05 times the particle size, molding,
The present invention relates to a method for producing a high-density graphite material, which is characterized by firing and graphitizing the material. The aggregate in the present invention is carbon material powder such as coke powder, graphite powder, oil smoke, etc., and the binding material is tar pitch, coal tar, etc. The average particle size of the aggregate is preferably 15 μm or less. If it exceeds 15 μm, the pore size in the structure becomes large, which is disadvantageous for achieving high density. It is preferable that the binding material has fixed carbon content of 35% by weight or more. If it is less than 35% by weight, a large amount of volatile matter is released, which is disadvantageous for achieving high density. The proportion of binder is preferably 25 to 60% by weight. If it is less than 25%, it is not sufficient to achieve high density, and if it exceeds 60%, kneading tends to be insufficient. The aggregate and binder are first thoroughly mixed using a V-type mixer or the like, or are thoroughly mixed during kneading. This mixture is kneaded using a double-armed mixer, a continuous mixer, etc., and the kneading temperature is set so that the kneaded product has an optimum viscosity. This kneading temperature is not particularly limited, but is generally 150 to 300℃.
It is. Kneading should be carried out sufficiently so that the aggregate and binder are uniform and the binder covers the aggregate well. Since the kneaded material obtained in this way is in the form of a lump, the maximum
It is necessary to coarsely grind to a particle size of mm or less. This is because if the kneaded material exceeds 10 mm, it will be difficult for the volatile matter to be removed during heat treatment, and the volatile matter will not be released uniformly between the inside and the surface. The kneaded material obtained in this way is heat-treated at a temperature of
Heat treatment is performed at 300-550℃. Heat treatment temperature is 300℃
Below, the release of volatiles is prolonged;
This is because if the temperature exceeds 550°C, the sintering properties of the kneaded material will almost disappear and the desired product will not be obtained. Heat treatment is possible even in an oxidizing atmosphere, but the treatment temperature is
If the temperature exceeds 350°C and the treatment time exceeds 40 minutes, oxidation will become significant and physical properties will deteriorate, so a non-oxidizing atmosphere is preferred. The heat treatment is preferably carried out so that the volatile content of the kneaded product is 5 to 20% by weight. This is because if the volatile content is less than 5%, the physical properties of the graphite material are insufficient, and if it exceeds 20%, blisters and cracks are likely to occur. The kneaded material after the heat treatment is pulverized by a pulverizer. Examples of the crusher include a ball mill, a vibrating ball mill, a jet mill, a turbo mill, a pin mill, etc., but are not particularly limited. The average particle size of the pulverized powder must be at least 1.05 times the aggregate particle size and 18 μm or less. If it is less than 1.05 times, the amount of binding material on the surface of the aggregate is insufficient, the binding strength decreases, and a high-density material cannot be obtained. Furthermore, if the average particle size of the pulverized powder exceeds 18 μm, the pore size in the structure becomes large and a high-density material cannot be obtained. This pulverized powder is molded into a predetermined shape by known means such as pressure molding or isostatic pressing to obtain a molded body, which is then fired by a known method in a firing furnace such as a Matsufuru furnace or a tunnel furnace, and further heated to 2500°C. Graphitization is performed at the above temperature, but these methods are not particularly limited. (Example) Next, an example will be described. Example 1 50 parts by weight of pitch coke powder with an average particle size of 3 μm,
50 parts by weight of tar pitch powder crushed to an average particle size of 35 μm was added and thoroughly mixed using a V-type mixer. This mixed powder was sufficiently kneaded using a double-armed milling machine while heating at a temperature of 200°C, and after cooling, it was coarsely ground to a maximum particle size of 4 mm or less. This was heated at 450° C. for 10 minutes in a nitrogen atmosphere to reduce the volatile content to 14% by weight. After coarsely pulverizing this kneaded material, it was pulverized in a ball mill until the average particle size became powder of 10 μm, and the molded product obtained by pressure molding was fired at about 1000°C in a non-oxidizing atmosphere, and graphite was heated at about 3000°C. It became. The physical properties at this time are shown in Table 1. Example 2 To 55 parts by weight of pitch coke powder having an average particle size of 3 μm, 45 parts by weight of tar pitch powder crushed to an average particle size of 35 μm was added and thoroughly mixed using a V-type mixer. This mixed powder was sufficiently kneaded while being heated at a temperature of 170° C. using a continuous milling machine, and after cooling, it was coarsely ground to a maximum particle size of 4 mm or less. This was done at 400℃ in a nitrogen atmosphere.
It was heated for 10 minutes to bring the volatile content to 16% by weight. After coarsely grinding this kneaded material, it was milled with a jet mill until the average particle size was 8 μm.
The molded body obtained by pressure molding is then sintered at approximately 1000℃ in a non-oxidizing atmosphere, resulting in approximately
Graphitization was performed at 3000℃. The physical properties at this time are shown in Table 1. Example 3 To 45 parts by weight of carbon black having an average particle size of 20 nm, 55 parts by weight of tar pitch powder crushed to an average particle size of 10 μm was added and thoroughly mixed using a V-type mixer. This mixed powder was thoroughly kneaded using a double-armed softener while heating at a temperature of 190°C, and after cooling, it was coarsely pulverized to obtain coarse particles with a maximum particle size of 4 mm or less. This is carried out in a nitrogen atmosphere.
It was heated at 450°C for 25 minutes to reduce the volatile content to 12% by weight.
This kneaded material was pulverized with a vibration mill until the average particle size was 6 μm, and the powder was pressure-molded to obtain a molded body, which was then fired at approximately 1000°C in a non-oxidizing atmosphere.
Graphitization was performed at 3000℃. The physical properties at this time are shown in Table 1. Comparative Example 1 35 parts by weight of ground tar pitch powder was added to 65 parts by weight of pitch coke powder with an average particle size of 25 μm, and V
Thoroughly mixed using a mold mixer. This mixed powder was kneaded for 3 hours while being heated at a temperature of 200° C. using a double-arm kneading machine. This kneaded material is pulverized and the average particle size is
It was set to 35 μm. The volatile content was 9%, and molding, firing, and graphitization were performed in the same manner as in Example 1. The physical properties are shown in Table 1. Comparative Example 1 The fired body obtained in Comparative Example 1 was impregnated with pitch, and after re-firing, it was graphitized in the same manner as in Example 1. Their physical properties are shown in Table 1. Example 4 40 parts by weight of tar pitch powder crushed to an average particle size of 35 μm was added to 60 parts by weight of pitch coke powder with an average particle size of 10 μm.
Parts by weight were added and thoroughly mixed using a mixer. This mixed powder is thoroughly kneaded while being heated at a temperature of 220°C using a continuous milling machine, and after cooling, it is coarsely pulverized to a maximum particle size of 4.
Coarse particles of less than mm were obtained. This was heated in the air at 350°C for 25 minutes to reduce the volatile content to 11% by weight. This kneaded material was ground with a vibration mill until the average particle size was 12 μm,
The pulverized powder was press-molded and then calcined at about 1000°C in a non-oxidizing atmosphere, and graphitized at a temperature of about 3000°C. Table 1 shows the values of the physical properties at this time.

【表】 第1表から明らかなように実施例の黒鉛材は比
較例の黒鉛材に比較してカサ密度が大きく、更に
曲げ強度及びシヨアー硬度も大きい。 (発明の効果) 本発明によれば、ピツチの含浸なしに、また高
価な装置を用いずに特性の優れた高密度黒鉛材を
経済的に得ることができ、本発明は、高密度を要
する放電加工用電極、連続鋳造用ノズル等の黒鉛
製品の製造に有効である。
[Table] As is clear from Table 1, the graphite materials of the examples have a larger bulk density and also have higher bending strength and shore hardness than the graphite materials of the comparative examples. (Effects of the Invention) According to the present invention, it is possible to economically obtain a high-density graphite material with excellent properties without pitch impregnation and without using expensive equipment. Effective for manufacturing graphite products such as electrodes for electrical discharge machining and nozzles for continuous casting.

Claims (1)

【特許請求の範囲】 1 骨材と結合材とを加熱混練し、最大粒径10mm
以下に粗粉砕した混練物を300〜550℃の温度で熱
処理し、次いで平均粒径が骨材の平均粒径の1.05
倍以上で18μm以下に粉砕した後、成形、焼成及
び黒鉛化することを特徴とする高密度黒鉛材の製
造法。 2 骨材が平均粒径15μm以下の骨材である特許
請求の範囲第1項記載の高密度黒鉛材の製造法。 3 熱処理が混練物の揮発分を5〜20重量%にす
る熱処理である特許請求の範囲第1項記載の高密
度黒鉛材の製造法。
[Claims] 1. Aggregate and binder are heated and kneaded to obtain a maximum particle size of 10 mm.
The coarsely pulverized kneaded material is heat treated at a temperature of 300 to 550℃, and then the average particle size is 1.05 of the average particle size of the aggregate.
A method for producing high-density graphite material, which comprises pulverizing the material to 18 μm or less by at least twice as much, followed by shaping, firing, and graphitization. 2. The method for producing a high-density graphite material according to claim 1, wherein the aggregate has an average particle size of 15 μm or less. 3. The method for producing a high-density graphite material according to claim 1, wherein the heat treatment is a heat treatment to reduce the volatile content of the kneaded material to 5 to 20% by weight.
JP59193263A 1984-09-14 1984-09-14 Production of high-density graphite material Granted JPS6172610A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59193263A JPS6172610A (en) 1984-09-14 1984-09-14 Production of high-density graphite material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59193263A JPS6172610A (en) 1984-09-14 1984-09-14 Production of high-density graphite material

Publications (2)

Publication Number Publication Date
JPS6172610A JPS6172610A (en) 1986-04-14
JPH0124724B2 true JPH0124724B2 (en) 1989-05-12

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP59193263A Granted JPS6172610A (en) 1984-09-14 1984-09-14 Production of high-density graphite material

Country Status (1)

Country Link
JP (1) JPS6172610A (en)

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CN113241438B (en) * 2021-05-10 2022-11-11 湖北亿纬动力有限公司 Negative electrode material and preparation method and application thereof
CN114314581B (en) * 2022-01-06 2023-06-30 河南佰利新能源材料有限公司 Preparation method of artificial graphite negative electrode material and lithium ion battery
WO2024224682A1 (en) * 2023-04-28 2024-10-31 Jfeスチール株式会社 Method for producing carbon briquette
EP4656618A1 (en) * 2023-04-28 2025-12-03 JFE Steel Corporation Method for producing carbonaceous lump

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JPS5383360A (en) * 1976-12-28 1978-07-22 Ibigawa Electric Ind Co Ltd Method of producing arc carbon electrode bar

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