JPH11100267A - Carbon material and its production - Google Patents

Carbon material and its production

Info

Publication number
JPH11100267A
JPH11100267A JP9260409A JP26040997A JPH11100267A JP H11100267 A JPH11100267 A JP H11100267A JP 9260409 A JP9260409 A JP 9260409A JP 26040997 A JP26040997 A JP 26040997A JP H11100267 A JPH11100267 A JP H11100267A
Authority
JP
Japan
Prior art keywords
powder
air
carbon material
amount
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.)
Pending
Application number
JP9260409A
Other languages
Japanese (ja)
Inventor
Yoshihiro Watanabe
美博 渡辺
Minoru Wada
稔 和田
Yasushi Komata
恭 小俣
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.)
Showa Denko Materials Co Ltd
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 JP9260409A priority Critical patent/JPH11100267A/en
Publication of JPH11100267A publication Critical patent/JPH11100267A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a static pressure air bearing eliminated in the need of controlling air permeating quantity by forming a carbon material having equal to or below a specific value of the dispersion of air passing quantity in the same block under a specific air pressure. SOLUTION: The carbon material has <=20 cm<3> /cm<2> /min dispersion of the air passing quantity in the same block under 0.469 MPa air pressure. The carbon material is obtained lay forming a kneaded material composed of 40-70 wt.% raw material aggregate powder containing >=80 wt.% particle having 1-60 μm particle diameter and 30-60 wt.% binder, mixing 1-20 wt.% organic material powder having 5-20 μmaverage particle diameter such as a resin bead having <=20% fixed carbon ratio, a pulp powder or the like with a pulverized powder obtained by pulverizing the kneaded material and having 50-100 μm average particle diameter to make a molding powder and firing a molding press molded under 600-1400 kg/cm<2> pressure in a reducing atmosphere at 800-1,000 deg.C for 300-500 hr. As the raw material aggregate, a coke powder, a graphite powder, a ccbon black or the like is used and as the binder, tar, pitch or the like is used.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、静圧空気軸受等の
カーボン摺動材として好適に用いられるカーボン材及び
その製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a carbon material suitably used as a carbon sliding material for a hydrostatic air bearing or the like, and a method for producing the same.

【0002】[0002]

【従来の技術】従来の静圧空気軸受製造技術として、特
開昭63−186030号公報に記載されているように
粒子径が40μm以下に分布した炭素材料用素材を成
形、焼成、黒鉛化して得られるカーボン材を用いること
が知られているが、このカーボン材は同一ブロック内の
空気透過量のバラツキが空気圧力0.49MPaにおい
て20cc/cm2/minを超え、静圧空気軸受に使
用する場合、空気透過量の調整が必要になるという問題
点があった。
2. Description of the Related Art As a conventional static pressure air bearing manufacturing technique, a material for a carbon material having a particle size distribution of 40 μm or less as described in JP-A-63-186030 is molded, fired and graphitized. It is known to use the obtained carbon material. However, this carbon material has a variation in the amount of air permeation in the same block exceeding 20 cc / cm 2 / min at an air pressure of 0.49 MPa, and is used for a hydrostatic air bearing. In such a case, there is a problem that the air permeation amount needs to be adjusted.

【0003】[0003]

【発明が解決しようとする課題】本発明の目的は、静圧
空気軸受に使用する場合、空気透過量のバラツキが小さ
いため空気透過量の調整が不要となり、生産性のよいカ
ーボン材を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a carbon material having a high productivity because when used in a hydrostatic air bearing, the variation in the amount of air permeation is small, so that it is not necessary to adjust the amount of air permeation. It is in.

【0004】本発明の他の目的は、上記の空気透過量の
バラツキが小さいカーボン材の好適な製造方法を提供す
ることにある。
Another object of the present invention is to provide a suitable method for producing a carbon material having a small variation in the amount of air permeation described above.

【0005】[0005]

【課題を解決するための手段】すなわち、本発明は、同
一ブロック内の空気透過量のバラツキが空気圧力0.4
9MPa(5kgf/cm2)において20cc/cm2
/min以下であるカーボン材を提供するものである。
That is, according to the present invention, the variation in the amount of air permeation in the same block is reduced to an air pressure of 0.4.
20 cc / cm 2 at 9 MPa (5 kgf / cm 2 )
/ Min or less.

【0006】本発明はまた、1〜60μmの粒径の粒子
を80重量%以上含有する原料骨材粉と結合材からなる
混練物(捏和物)を粉砕して得られる粉砕粉を含有する
成形粉を成形し、焼成することを特徴とする上記のカー
ボン材の好適な製造方法を提供するものである。
The present invention also includes a ground powder obtained by grinding a kneaded product (kneaded product) comprising a raw material aggregate powder containing at least 80% by weight of particles having a particle size of 1 to 60 μm and a binder. An object of the present invention is to provide a suitable method for producing the above-mentioned carbon material, which comprises molding and firing a molding powder.

【0007】[0007]

【発明の実施の形態】本発明のカーボン材は、同一ブロ
ック内の空気透過量のバラツキが空気圧力0.49MP
aにおいて20cc/cm2/min以下と小さいた
め、静圧空気軸受に使用した場合、空気透過量の調整が
不要であり、品質の安定した軸受を生産性よく製造する
ことができる。前記空気透過量のバラツキが20cc/
cm2/minより大きいと、空気透過量調整作業が煩
雑で、品質の安定化に時間を要する。前記の空気透過量
のバラツキは15cc/cm2/min以下であるとよ
り好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION In the carbon material of the present invention, the variation in the amount of air permeation in the same block is 0.49MPa.
Since a is as small as 20 cc / cm 2 / min or less in a, when used for a hydrostatic air bearing, it is not necessary to adjust the amount of air permeation, and a bearing of stable quality can be manufactured with high productivity. The variation of the air permeation amount is 20 cc /
If it is larger than cm 2 / min, the work of adjusting the amount of air permeation is complicated, and it takes time to stabilize the quality. More preferably, the variation of the air permeation amount is 15 cc / cm 2 / min or less.

【0008】ここで同一ブロック内とは、金型プレス、
ラバープレス等で賦形され、製造されたカーボン材の1
つの成形体ブロック内を意味し、同一ブロック内での空
気透過量のバラツキは、できる限りブロックの全体から
サンプルを多く抽出して測定することが好ましい。具体
的方法としては、製造したブロックを高さ方向に上部、
中部、下部と三等分した3つのそれぞれの範囲におい
て、水平方向にみて中心部、中間部、外縁部の3箇所、
合計9箇所のサンプルを抽出し、空気透過量を測定し、
その最大値と最小値の差をもってバラツキとすることが
好ましい。
Here, in the same block, a mold press,
One of the carbon materials manufactured and shaped by rubber press etc.
It means within one molded block, and it is preferable to measure the variation in the amount of air permeation in the same block by extracting as many samples as possible from the entire block. As a specific method, the manufactured block is placed in the upper part in the height direction,
In each of the three ranges divided into three parts, the middle part, the lower part, and the central part, the middle part, and the outer edge part when viewed in the horizontal direction,
Extract a total of 9 samples, measure the amount of air permeation,
It is preferable that the difference is obtained based on the difference between the maximum value and the minimum value.

【0009】空気透過量は、サンプルをそれぞれ、ブロ
ックの成形加圧方向(金型プレスの場合)又は成形時の
重力方向(ラバープレスの場合)を200mmとした4
50mm×450mm×200mmの大きさの直方体に
切り出し、図2示す空気透過量測定装置に、前記成形加
圧方向(金型プレスの場合)又は成形時の重力方向(ラ
バープレスの場合)に対して垂直方向の空気透過量を測
定するようにサンプルを固定し、0.49MPa(5k
gf/cm2)の圧力を加えて測定することができる。
測定される空気透過量の単位は、cc/cm2/min
であるが、これは1cm2の面積当たりで、1分間に透
過する空気体積(cc)を意味する。図2において5は
試験片、6は空気ボンベ、7は圧力ゲージ、8は流量メ
ーターを示す。
The amount of air permeation was determined by setting the sample to 200 mm in the block pressing direction (in the case of a die press) or in the direction of gravity during molding (in the case of a rubber press).
A rectangular parallelepiped having a size of 50 mm × 450 mm × 200 mm is cut out and is measured by the air permeation amount measuring apparatus shown in FIG. The sample was fixed so as to measure the amount of air permeation in the vertical direction.
gf / cm 2 ).
The unit of the measured air permeation amount is cc / cm 2 / min.
Although, this is a per area of 1 cm 2, which means a volume of air which passes per minute (cc). In FIG. 2, 5 indicates a test piece, 6 indicates an air cylinder, 7 indicates a pressure gauge, and 8 indicates a flow meter.

【0010】本発明のカーボン材を製造するには、成形
粉として、1〜60μmの粒径の粒子を80重量%以
上、好ましくは90重量%以上含有する原料骨材粉と結
合材からなる混練物(捏和物)を粉砕して得られる粉砕
粉を含有するものを用いることが好ましい。原料骨材粉
中の1〜60μmの粒径の粒子が80重量%未満だと得
られるカーボン材の空気透過量のバラツキが大きくなる
傾向にある。
In order to produce the carbon material of the present invention, kneading is carried out by using a raw material aggregate powder containing particles having a particle size of 1 to 60 μm as 80% by weight or more, preferably 90% by weight or more and a binder as molding powder. It is preferable to use one containing a pulverized powder obtained by pulverizing a product (kneaded product). If the particles having a particle diameter of 1 to 60 μm in the raw material aggregate powder are less than 80% by weight, the air permeation amount of the obtained carbon material tends to vary widely.

【0011】原料骨材としては、好ましくは、コークス
粉、黒鉛粉、カーボンブラック等が用いられる。結合材
としては、好ましくは、タール、ピッチ等が用いられ
る。
As the raw material aggregate, preferably, coke powder, graphite powder, carbon black or the like is used. Preferably, tar, pitch or the like is used as the binder.

【0012】原料骨材粉の捏和物中の配合割合は、40
〜70重量%とすることが好ましい。また、捏和物中の
結合材の配合割合は、30〜60重量%とすることが好
ましい。
The mixing ratio of the raw material aggregate powder in the kneaded product is 40
It is preferable to set it to 70% by weight. Further, the mixing ratio of the binder in the kneaded product is preferably set to 30 to 60% by weight.

【0013】本発明に用いられる成形粉としては、上記
捏和物を粉砕して得られる粉砕粉をそのまま用いること
ができるが、この粉砕粉にさらに有機物粉末を配合した
ものを用いることが好ましい。
As the molding powder used in the present invention, a pulverized powder obtained by pulverizing the above kneaded material can be used as it is, but it is preferable to use a powder obtained by further mixing an organic substance powder with the pulverized powder.

【0014】成形粉に配合される有機物粉末としては、
特に制限はないが、樹脂ビーズ、でんぷん粉、パルプ粉
等が好適に用いられる。樹脂ビーズとしては好ましくは
ポリメタクリル酸メチルビーズが用いられる。有機物粉
末は固定炭素率が20%以下のものが好ましく用いられ
る。20%を超えると、通気孔の形成が不十分となる傾
向がある。ここで固定炭素率とは、JIS K 242
1に準拠した有機物を還元雰囲気中で800℃で焼成
し、残った炭素質物量を意味する。
As the organic powder to be mixed with the molding powder,
Although there is no particular limitation, resin beads, starch powder, pulp powder and the like are preferably used. Polymethyl methacrylate beads are preferably used as the resin beads. Organic powder having a fixed carbon ratio of 20% or less is preferably used. If it exceeds 20%, the formation of air holes tends to be insufficient. Here, the fixed carbon ratio refers to JIS K242
1 means the amount of carbonaceous material remaining after firing an organic substance at 800 ° C. in a reducing atmosphere.

【0015】また、有機物粉末は平均粒径が5〜20μ
mのものが好ましい。20μmより大きいと空気透過量
のバラツキが大きくなる傾向があり、5μmより小さい
と分散が悪くなり気孔分布が不均質な組織となる傾向が
ある。さらに、その配合量は、成形粉に対して1〜20
重量%の範囲とすることが好ましい。20重量%より多
いと強度が低下し構造材とし不適となる傾向がある。ま
た、1%より少ないと、通気孔形成が不十分となる傾向
がある。
The organic powder has an average particle size of 5 to 20 μm.
m is preferred. If it is larger than 20 μm, the variation in the amount of air permeation tends to increase, and if it is smaller than 5 μm, the dispersion tends to be poor and the pore distribution tends to be uneven. Furthermore, the compounding amount is 1 to 20 with respect to the molding powder.
It is preferably in the range of% by weight. If the content is more than 20% by weight, the strength tends to decrease and the material tends to be unsuitable as a structural material. If it is less than 1%, the formation of air holes tends to be insufficient.

【0016】原料骨材粉と結合材とを捏和、粉砕するこ
とにより粉砕粉が得られる。捏和は、一般に双腕型ニー
ダー等を用いて、各材料を好ましくは200〜250℃
で好ましくは5〜10時間混練することにより行われ
る。
A kneaded powder is obtained by kneading and pulverizing the raw material aggregate powder and the binder. The kneading is generally performed using a double-arm kneader or the like, and each material is preferably 200 to 250 ° C.
And preferably by kneading for 5 to 10 hours.

【0017】粉砕は、捏和で得られた捏和物を各種粉砕
機を用いて平均粒子径が好ましくは20〜30μmにな
るように粉砕することにより行われる。
The pulverization is carried out by pulverizing the kneaded product obtained by kneading using various pulverizers so that the average particle diameter is preferably 20 to 30 μm.

【0018】粉砕粉は造粒して用いることが好ましく、
捏和物を粉砕して得られる粉砕粉を平均粒径は50〜1
00μmに造粒することが好ましい。100μmより大
きいと空気透過量のバラツキが大きくなる傾向がある。
50μmより小さいと、造粒作業に時間を要する傾向が
ある。
The ground powder is preferably granulated and used.
The pulverized powder obtained by pulverizing the kneaded product has an average particle size of 50 to 1
It is preferable to granulate to 00 μm. If it is larger than 100 μm, the variation in the amount of air permeation tends to increase.
If it is smaller than 50 μm, the granulating operation tends to take a long time.

【0019】粉砕粉と有機粉末との混合は、各種混合機
で好ましくは10〜30分混合することにより行われ
る。
The mixing of the pulverized powder and the organic powder is carried out by various mixers, preferably for 10 to 30 minutes.

【0020】成形粉の造粒は、各種噴霧急速乾燥式造粒
機を用いて、造粒平均粒径が50〜100μmになるよ
うに造粒することにより行われる。
The granulation of the molding powder is carried out by using various types of spray-drying-type granulators so that the average granulated particle diameter is 50 to 100 μm.

【0021】成形は、粉砕により得られ粉体又は造粒に
より得られた粉体を含む成形粉を、ブロック状にラバー
プレス、金型プレス等の方法で、賦形することにより行
われる。このときの圧力は、600〜1400kg/c
2が好ましい。低いと得られた成形品の比重が下が
り、高いと焼成中に割れやすくなる傾向がある。
The compacting is performed by shaping the compacted powder containing the powder obtained by pulverization or the powder obtained by granulation by a method such as a rubber press or a mold press. The pressure at this time is 600 to 1400 kg / c.
m 2 is preferred. When it is low, the specific gravity of the obtained molded article decreases, and when it is high, it tends to be easily cracked during firing.

【0022】上記により得られた成形品を、焼成し、さ
らに用途に応じて黒鉛化することにより目的とするカー
ボン材が得られる。
The molded product obtained as described above is fired, and further graphitized according to the intended use to obtain the desired carbon material.

【0023】焼成は、還元雰囲気下、好ましくは800
〜1000℃に昇温して、行うことができる。焼成時間
は、300〜500時間が好ましい。還元雰囲気下で焼
成する方法としては、成形体のまわりに炭素粉を詰めて
焼成する方法等がある。
The calcination is carried out under a reducing atmosphere, preferably 800
The temperature can be raised to 10001000 ° C. The firing time is preferably 300 to 500 hours. As a method for firing in a reducing atmosphere, there is a method in which carbon powder is packed around a molded body and fired.

【0024】こうして得られるカーボン材は、カーボン
摺動材として、カーボンベーン、シールパッキング、軸
受等に用いられる。中でも静圧空気軸受用として好適で
ある。
The carbon material thus obtained is used as a carbon sliding material for carbon vanes, seal packing, bearings and the like. Among them, it is suitable for a hydrostatic air bearing.

【0025】[0025]

【実施例】以下、本発明を実施例に基づいて詳細に説明
するが、本発明はこれに限定されるものではない。
The present invention will be described below in detail with reference to examples, but the present invention is not limited to these examples.

【0026】実施例1 骨材として平均粒径15〜25μmで1〜60μmの粒
径の粒子を95重量%含む自家製黒鉛粉45重量%とカ
ーボンブラック(カンカーブ社製、商品名サーマック
ス)10重量%の混合物にバインダピッチ(川崎製鉄
製、商品名PKE)44重量%を配合し、温度240℃
で3時間混練した。この捏和物を平均粒径25μmに粉
砕し成形粉とした。この成形粉をφ150×150mm
の円筒状のゴム型に封入し、1000kgf/cm2
ラバープレス成形した。得られた成形品を、還元雰囲気
下、室温から1000℃まで100時間で昇温し焼成し
た。得られた焼成品から特性測定用のサンプルを図1に
示す採取位置から採取し、物理特性と空気透過量を測定
した。空気透過量サンプルは図1に示す中間、中心、外
周位置について上、中、下の計9か所から前述の方法に
従って、物理特性用サンプルは図1に示す3か所からサ
ンプルを得た(以下同様)。
Example 1 45% by weight of a home-made graphite powder containing 95% by weight of particles having an average particle diameter of 15 to 25 μm and a particle diameter of 1 to 60 μm as an aggregate, and 10% by weight of carbon black (trade name, trade name, manufactured by Can Curve) % Blended with 44% by weight of binder pitch (manufactured by Kawasaki Steel, PKE) at a temperature of 240 ° C.
For 3 hours. This kneaded product was pulverized to an average particle size of 25 μm to obtain a molding powder. This molding powder is φ150 × 150mm
And rubber-pressed at 1000 kgf / cm 2 . The obtained molded article was heated from room temperature to 1000 ° C. for 100 hours in a reducing atmosphere and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured. According to the above-described method, the air permeation amount samples were obtained from a total of nine locations, that is, the middle, center, and outer peripheral positions shown in FIG. Hereinafter the same).

【0027】その結果、空気透過量のバラツキ(最大値
−最小値)は18cc/cm2/minであった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 18 cc / cm 2 / min.

【0028】実施例2 実施例1で得られた成形粉90重量%に樹脂ビーズ(ポ
リメタクリル酸メチルビーズ、平均粒径5μm)10重
量%を混合撹拌して成形粉を得た。この成形粉をφ15
0×150mmの円筒状のゴム型に封入し、1000k
gf/cm2でラバープレス成形した。得られた成形品
を、、還元雰囲気下、室温から1000℃まで100時
間で昇温し焼成した。得られた焼成品から特性測定用の
サンプルを図1に示す採取位置から採取し、物理特性と
空気透過量を測定した。
EXAMPLE 2 10% by weight of resin beads (polymethyl methacrylate beads, average particle size: 5 μm) were mixed and stirred with 90% by weight of the molding powder obtained in Example 1 to obtain a molding powder. This molding powder is φ15
Sealed in 0x150mm cylindrical rubber mold, 1000k
Rubber press molding was performed at gf / cm 2 . The obtained molded product was heated from room temperature to 1000 ° C. for 100 hours in a reducing atmosphere and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0029】その結果、空気透過量のバラツキ(最大値
−最小値)は11cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 11 cc / cm 2 / min.

【0030】実施例3 実施例1で得られた成形粉90重量%に樹脂ビーズ(ポ
リメタクリル酸メチルビーズ、平均粒径10μm)10
重量%を混合撹拌して成形粉を得た。この成形粉をφ1
50×150mmの円筒状のゴム型に封入し、1000
kgf/cm2でラバープレス成形した。得られた成形
品を、還元雰囲気下、室温から1000℃まで100時
間で昇温し焼成した。得られた焼成品から特性測定用の
サンプルを図1に示す採取位置から採取し、物理特性と
空気透過量を測定した。
Example 3 Resin beads (polymethyl methacrylate beads, average particle size: 10 μm) were added to 90% by weight of the molding powder obtained in Example 1.
The mixture was stirred by weight to obtain a molding powder. This molding powder is φ1
Sealed in a 50 × 150 mm cylindrical rubber mold, 1000
Rubber press molding was performed at kgf / cm 2 . The obtained molded article was heated from room temperature to 1000 ° C. for 100 hours in a reducing atmosphere and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0031】その結果、空気透過量のバラツキ(最大値
−最小値)は12cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 12 cc / cm 2 / min.

【0032】実施例4 実施例1で得られた成形粉90重量%にでんぷん粉(サ
イデン化学(株)製、商品名サイビノール、平均粒径1
0μm)10重量%を混合撹拌して成形粉を得た。この
成形粉をφ150×150mmの円筒状のゴム型に封入
し、1000kgf/cm2でラバープレス成形した。
得られた成形品を、還元雰囲気下、室温から1000℃
まで100時間で昇温し焼成した。得られた焼成品から
特性測定用のサンプルを図1に示す採取位置から採取
し、物理特性と空気透過量を測定した。
Example 4 90% by weight of the molding powder obtained in Example 1 was added to starch (manufactured by Seiden Chemical Co., Ltd., trade name Cybinol, average particle size 1).
(0 μm) and 10% by weight were mixed and stirred to obtain a molding powder. This molding powder was sealed in a cylindrical rubber mold of φ150 × 150 mm and subjected to rubber press molding at 1000 kgf / cm 2 .
The obtained molded article is heated from room temperature to 1000 ° C. in a reducing atmosphere.
The temperature was raised for 100 hours until firing. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0033】その結果、空気透過量のバラツキ(最大値
−最小値)は15cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 15 cc / cm 2 / min.

【0034】実施例5 実施例1で得られた成形粉90重量%にパルプ粉末(山
陽国策パルプ(株)製、KCフロック#400、平均粒
径20μm)10重量%を混合撹拌して成形粉を得た。
この成形粉をφ150×150mmの円筒状のゴム型に
封入し、1000kgf/cm2でラバープレス成形し
た。得られた成形品を、還元雰囲気下、室温から100
0℃まで100時間で昇温し焼成した。得られた焼成品
から特性測定用のサンプルを図1に示す採取位置から採
取し、物理特性と空気透過量を測定した。
EXAMPLE 5 10% by weight of pulp powder (KC Floc # 400, average particle size 20 μm, manufactured by Sanyo Kokusaku Pulp Co., Ltd.) was mixed and stirred with 90% by weight of the molding powder obtained in Example 1 to form a molding powder. I got
This molding powder was sealed in a cylindrical rubber mold of φ150 × 150 mm and subjected to rubber press molding at 1000 kgf / cm 2 . The obtained molded product is reduced from room temperature to 100
The temperature was raised to 0 ° C. for 100 hours and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0035】その結果、空気透過量のバラツキ(最大値
−最小値)は18cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 18 cc / cm 2 / min.

【0036】実施例6 実施例1で得られた成形粉を噴霧急速乾燥式造粒機にか
け、造粒粉平均粒径70μmの成形粉を得た。この成形
粉をφ150×150mmの円筒状のゴム型に封入し、
1000kgf/cm2でラバープレス成形した。得ら
れた成形品を、還元雰囲気下、室温から1000℃まで
100時間で昇温し焼成した。得られた焼成品から特性
測定用のサンプルを図1に示す採取位置から採取し、物
理特性と空気透過量を測定した。
Example 6 The molding powder obtained in Example 1 was applied to a spray-drying granulator to obtain a molding powder having an average particle diameter of 70 μm. This molding powder is sealed in a cylindrical rubber mold of φ150 × 150 mm,
Rubber press molding was performed at 1000 kgf / cm 2 . The obtained molded article was heated from room temperature to 1000 ° C. for 100 hours in a reducing atmosphere and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0037】その結果、空気透過量のバラツキ(最大値
−最小値)は14cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 14 cc / cm 2 / min.

【0038】比較例1 骨材として平均粒径15〜25μmで1〜60μmの粒
径の粒子を60重量%含む自家製黒鉛粉45重量%とカ
ーボンブラック(カンカーブ社製、商品名サーマック
ス)10重量%の混合物にバインダピッチ(川崎製鉄
製、商品名PKE)44重量%を配合し、温度240℃
で3時間混練した。この捏和物を平均粒径25μmに粉
砕し成形粉を得た。この成形粉をφ150×150mm
の円筒状のゴム型に封入し、1000kgf/cm2
ラバープレス成形した。得られた成形品を、還元雰囲気
下、室温から1000℃まで100時間で昇温し焼成し
た。得られた焼成品から特性測定用のサンプルを図1に
示す採取位置から採取し、物理特性と空気透過量を測定
した。
Comparative Example 1 45% by weight of self-made graphite powder containing 60% by weight of particles having an average particle diameter of 15 to 25 μm and 1 to 60 μm as an aggregate, and 10% by weight of carbon black (trade name, trade name, manufactured by Cancarb Corp.) % Blended with 44% by weight of binder pitch (manufactured by Kawasaki Steel, PKE) at a temperature of 240 ° C.
For 3 hours. This kneaded product was pulverized to an average particle size of 25 μm to obtain a molded powder. This molding powder is φ150 × 150mm
And rubber-pressed at 1000 kgf / cm 2 . The obtained molded article was heated from room temperature to 1000 ° C. for 100 hours in a reducing atmosphere and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0039】その結果、空気透過量のバラツキ(最大値
−最小値)は30cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 30 cc / cm 2 / min.

【0040】比較例2 骨材として平均粒径15〜25μmで1〜60μmの粒
径の粒子を70重量%含む自家製黒鉛粉45重量%とカ
ーボンブラック(カンカーブ社製、商品名サーマック
ス)10重量%の混合物にバインダピッチ(川崎製鉄
製、商品名PKE)44重量%を配合し、温度240℃
で2時間混練した。この捏和物を平均粒径25μmに粉
砕し成形粉を得た。この成形粉70重量%にパルプ粉末
(山陽国策パルプ(株)製、KCフロック#400、粒
径20μm)10重量%を混合撹拌して成形粉を得た。
この成形粉をφ150×150mmの円筒状のゴム型に
封入し、1000kgf/cm2でラバープレス成形し
た。得られた成形品を、還元雰囲気下、室温から100
0℃まで100時間で昇温し焼成した。得られた焼成品
から特性測定用のサンプルを図1に示す採取位置から採
取し、物理特性と空気透過量を測定した。
Comparative Example 2 45% by weight of a homemade graphite powder containing 70% by weight of particles having an average particle size of 15 to 25 μm and a particle size of 1 to 60 μm as an aggregate and 10% by weight of carbon black (trade name, manufactured by Cancarb Corp.) % Blended with 44% by weight of binder pitch (manufactured by Kawasaki Steel, PKE) at a temperature of 240 ° C.
For 2 hours. This kneaded product was pulverized to an average particle size of 25 μm to obtain a molded powder. 10% by weight of pulp powder (KC Floc # 400, manufactured by Sanyo Kokusaku Pulp Co., Ltd., particle size: 20 μm) was mixed and stirred with 70% by weight of this molding powder to obtain a molding powder.
This molding powder was sealed in a cylindrical rubber mold of φ150 × 150 mm and subjected to rubber press molding at 1000 kgf / cm 2 . The obtained molded product is reduced from room temperature to 100
The temperature was raised to 0 ° C. for 100 hours and fired. A sample for property measurement was collected from the obtained baked product from the collection position shown in FIG. 1, and the physical properties and the amount of air permeation were measured.

【0041】その結果、空気透過量のバラツキ(最大値
−最小値)は35cc/cm2/min であった。
As a result, the variation (maximum value-minimum value) of the air permeation amount was 35 cc / cm 2 / min.

【0042】[0042]

【表1】 バラツキ=最大値−最小値 表1に示すように、実施例1〜6の空気透過量のバラツ
キは、比較例より小さく、制御されていた。
[Table 1] Variation = maximum value−minimum value As shown in Table 1, the variation of the air permeation amount of Examples 1 to 6 was smaller than that of the comparative example and was controlled.

【0043】[0043]

【発明の効果】本発明により、静圧空気軸受に使用する
場合、空気透過量のバラツキが小さいため空気透過量の
調整が不要となるカーボン摺動材が得られた。このカー
ボン摺動材を用いると静圧空気軸受作製時の空気透過量
調整工程の時間短縮ができ、得られた製品の品質が安定
する。
According to the present invention, a carbon sliding material which does not require adjustment of the amount of air permeation when used in a hydrostatic air bearing because the variation of the amount of air permeation is small is obtained. The use of this carbon sliding material can reduce the time required for the air permeation adjustment step when producing a hydrostatic air bearing, and stabilizes the quality of the obtained product.

【図面の簡単な説明】[Brief description of the drawings]

【図1】サンプルの採取位置を示す説明図FIG. 1 is an explanatory diagram showing a sampling position of a sample.

【図2】空気透過量測定装置の概略図FIG. 2 is a schematic diagram of an air permeation amount measuring device

【符号の説明】[Explanation of symbols]

1 空気透過量サンプル位置(中間) 2 空気透過量サンプル位置(中心) 3 空気透過量サンプル位置(外周) 4 物理特性用サンプル位置 5 試験片 6 空気ボンベ 7 圧力ゲージ 8 流量メーター 1 Air permeation amount sample position (middle) 2 Air permeation amount sample position (center) 3 Air permeation amount sample position (outer periphery) 4 Physical property sample position 5 Test piece 6 Air cylinder 7 Pressure gauge 8 Flow meter

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 同一ブロック内の空気透過量のバラツキ
が空気圧力0.49MPaにおいて20cc/cm2
min以下であるカーボン材。
1. The variation in the amount of air permeation in the same block is 20 cc / cm 2 / at an air pressure of 0.49 MPa.
min or less carbon material.
【請求項2】 1〜60μmの粒径の粒子を80重量%
以上含有する原料骨材粉と結合材からなる混練物を粉砕
して得られる粉砕粉を含有する成形粉を成形し、焼成す
ることを特徴とする請求項1記載のカーボン材の製造方
法。
2. 80% by weight of particles having a particle size of 1 to 60 μm.
2. The method for producing a carbon material according to claim 1, wherein a molding powder containing a pulverized powder obtained by pulverizing a kneaded product comprising the raw material aggregate powder and the binder contained above is molded and fired.
【請求項3】 1〜60μmの粒径の粒子を80重量%
以上含有する原料骨材粉と結合材からなる混練物を粉砕
して得られる粉砕粉に有機物粉末を1〜20重量%含有
させた成形粉を成形し、焼成することを特徴とする請求
項1記載のカーボン材の製造方法。
3. 80% by weight of particles having a particle size of 1 to 60 μm.
2. A molding powder obtained by pulverizing a kneaded product composed of the above-mentioned raw material aggregate powder and a binder and comprising a powder obtained by containing 1 to 20% by weight of an organic powder in a pulverized powder, followed by firing. A method for producing the carbon material as described above.
【請求項4】 粉砕粉が平均粒径50〜100μmに造
粒されたものである請求項2又は3記載のカーボン材の
製造方法。
4. The method for producing a carbon material according to claim 2, wherein the pulverized powder is granulated to have an average particle size of 50 to 100 μm.
JP9260409A 1997-09-25 1997-09-25 Carbon material and its production Pending JPH11100267A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9260409A JPH11100267A (en) 1997-09-25 1997-09-25 Carbon material and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9260409A JPH11100267A (en) 1997-09-25 1997-09-25 Carbon material and its production

Publications (1)

Publication Number Publication Date
JPH11100267A true JPH11100267A (en) 1999-04-13

Family

ID=17347533

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9260409A Pending JPH11100267A (en) 1997-09-25 1997-09-25 Carbon material and its production

Country Status (1)

Country Link
JP (1) JPH11100267A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013001576A (en) * 2011-06-10 2013-01-07 Ibiden Co Ltd Method for producing graphite material, and graphite material
JP2020152902A (en) * 2019-03-19 2020-09-24 関西熱化学株式会社 Carbon black molded body and method for producing the same
CN117447204A (en) * 2023-12-22 2024-01-26 成都中超碳素科技有限公司 Preparation method of mechanical carbon material

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013001576A (en) * 2011-06-10 2013-01-07 Ibiden Co Ltd Method for producing graphite material, and graphite material
US8980787B2 (en) 2011-06-10 2015-03-17 Ibiden Co., Ltd. Method for producing graphite material and graphite material
JP2020152902A (en) * 2019-03-19 2020-09-24 関西熱化学株式会社 Carbon black molded body and method for producing the same
CN117447204A (en) * 2023-12-22 2024-01-26 成都中超碳素科技有限公司 Preparation method of mechanical carbon material
CN117447204B (en) * 2023-12-22 2024-03-15 成都中超碳素科技有限公司 Preparation method of mechanical carbon material

Similar Documents

Publication Publication Date Title
EP0254551B1 (en) Process for the production of porous shaped articles
WO2011040344A1 (en) Method for producing briquettes, method for producing reduced metal, and method for separating zinc or lead
JP2019512454A (en) Method for producing coal-based shaped activated carbon containing no binder
KR101302765B1 (en) Briquette manufacturing method, reductive metal manufacturing method, and zinc or lead separation method
JPS6223642B2 (en)
EP3402590A1 (en) Process and system for the dry granulation of powdered ceramic mixture
JPH11100267A (en) Carbon material and its production
JP2008536792A (en) Method for compacting hydraulic binder and novel pulverized pellets
CN103011854B (en) Method for processing raw material of isostatic pressing clay-graphite crucible
JPH04367578A (en) Porous sintered compact and its production
EP0277708A2 (en) Pellet fabrication
WO2020203825A1 (en) Method for manufacturing high-density artificial graphite electrode
US20210355395A1 (en) Process for coal fine aggregation
JPH05238716A (en) Method for kneading special carbon material
JPS58208113A (en) Manufacture of isotropic graphite body
RU2740392C1 (en) Method of producing silicon carbide refractories
JPS593511B2 (en) Method for producing small pellets using fine coke
KR102243573B1 (en) Coal briquet composition using a soluble binder and method for producing the same
JP3711247B2 (en) Filter element
RU2199161C2 (en) Method for producing nuclear fuel pellets primarily for fast reactors
CN115893905A (en) Grinding aid and preparation method thereof
JPS63170254A (en) Manufacture of ceramics
SU1654358A1 (en) Method of manufacture of sintered metallic filters
JP2000266056A (en) Carbon sliding material and manufacture thereof
JPH03290310A (en) Production of active carbon

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20040812

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070104

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080122

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20080722