JPH05246765A - Compact for producing cubic boron nitride sintered compact - Google Patents

Compact for producing cubic boron nitride sintered compact

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Publication number
JPH05246765A
JPH05246765A JP4080403A JP8040392A JPH05246765A JP H05246765 A JPH05246765 A JP H05246765A JP 4080403 A JP4080403 A JP 4080403A JP 8040392 A JP8040392 A JP 8040392A JP H05246765 A JPH05246765 A JP H05246765A
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JP
Japan
Prior art keywords
compact
catalyst
boron nitride
cubic boron
air permeability
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.)
Granted
Application number
JP4080403A
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Japanese (ja)
Other versions
JP2715794B2 (en
Inventor
Toshihiko Shindo
敏彦 進藤
Toshiyuki Murayama
俊幸 村山
Yutaka Sato
豊 佐藤
Shu Kashida
周 樫田
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Shin Etsu Chemical Co Ltd
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Shin Etsu Chemical Co Ltd
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Priority to JP4080403A priority Critical patent/JP2715794B2/en
Publication of JPH05246765A publication Critical patent/JPH05246765A/en
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Publication of JP2715794B2 publication Critical patent/JP2715794B2/en
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Expired - Fee Related legal-status Critical Current

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Abstract

(57)【要約】 【構成】 通気率が0.01〜0.3cm2/secの
六方晶窒化ホウ素成形体に立方晶窒化ホウ素化触媒を含
浸してなることを特徴とする立方晶窒化ホウ素焼結体製
造用成形体を提供する。 【効果】 本発明によれば、h−BN成形体へのc−B
N化触媒含浸が容易かつ均一になり、h−BN成形体が
厚肉である場合でも中心部まで安定して均一良好に触媒
が含浸する。このため、厚肉のc−BN焼結体を高品質
に歩留まりよく製造することができる。
(57) [Summary] [Structure] A cubic boron nitride characterized by being formed by impregnating a hexagonal boron nitride molded body having an air permeability of 0.01 to 0.3 cm 2 / sec with a cubic boron nitriding catalyst. Provided is a molded body for producing a sintered body. [Effects] According to the present invention, c-B to h-BN compacts is obtained.
Impregnation of the N-ized catalyst becomes easy and uniform, and even when the h-BN compact is thick, the catalyst is stably and uniformly impregnated to the center portion. Therefore, a thick c-BN sintered body can be manufactured with high quality and high yield.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、立方晶窒化ホウ素焼結
体を高純度、高密度、高硬度でかつ歩留まりよく製造す
ることができる立方晶窒化ホウ素焼結体製造用成形体に
関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a cubic boron nitride sintered compact for producing a cubic boron nitride sintered compact with high purity, high density, high hardness and high yield.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】立方晶
窒化ホウ素(以下、c−BNと略記する。)はダイヤモ
ンドに匹敵する高い硬度と化学的な安定性を有している
ため、高速度、高精度加工用工業材料として使用されて
いるほか、その極めて良好な熱伝導性からヒートシンク
材等に利用されており、また、半導体特性等を有するこ
とから電子材料などへの応用も進んでいる。
BACKGROUND OF THE INVENTION Cubic boron nitride (hereinafter abbreviated as c-BN) has a high hardness and chemical stability comparable to diamond, and therefore has a high speed. In addition to being used as an industrial material for high-precision processing, it is also used as a heat sink material due to its extremely good thermal conductivity, and is also being applied to electronic materials because of its semiconductor properties. ..

【0003】このような特性を十分に発揮するために
は、c−BNは高純度、高密度の焼結体であることが要
求される。このようなc−BN焼結体は、一般的には六
方晶窒化ホウ素(以下、h−BNと略記する。)粉末を
出発原料とし、高温高圧条件下でc−BNに変換するこ
とにより製造されているが、このような高温高圧条件下
でのc−BNの変換は、製造装置が大型化し、また、製
造条件の制御も難しいものとなる。
In order to fully exhibit such characteristics, c-BN is required to be a high-purity, high-density sintered body. Such a c-BN sintered body is generally produced by using hexagonal boron nitride (hereinafter abbreviated as h-BN) powder as a starting material and converting it into c-BN under high temperature and high pressure conditions. However, in the conversion of c-BN under such high temperature and high pressure conditions, a manufacturing apparatus becomes large and it is difficult to control the manufacturing conditions.

【0004】そこで、このような問題点を解決した製造
方法として、特公昭59−5547号公報において、窒
化ホウ素にM324(Mはアルカリ土類金属を表わ
す。)等の触媒物質を混合した出発原料を用い、上記の
製造方法よりも低温低圧条件下においてc−BNを製造
する方法が提案されている。
Therefore, as a manufacturing method for solving such a problem, in Japanese Patent Publication No. 59-5547, a catalyst material such as M 3 B 2 N 4 (M represents an alkaline earth metal) in boron nitride is used. There is proposed a method for producing c-BN under a condition of low temperature and low pressure as compared with the above-mentioned production method, using a starting material mixed with.

【0005】また、特公昭60−28782号公報にお
いて、ホットプレス法により製造されたh−BN成形体
に上記触媒を拡散含浸させたものを前駆体に用いてc−
BN焼結体を製造する方法も提案されている。
Further, in Japanese Patent Publication No. 60-28782, a h-BN molded body produced by a hot pressing method, which is obtained by diffusing and impregnating the above catalyst with a catalyst, is used as a precursor.
A method of manufacturing a BN sintered body has also been proposed.

【0006】しかし、本発明者は、ホットプレス法で製
造されたh−BN成形体においてはh−BN粒子同士が
その接触部で密接して接合しており、また、B 23等の
酸化物が原料粉末の表面に多く存在するほどその接合強
度も高くなり、このため、空隙率の高い、密度が1.8
g/cm3以下の低密度成形体を用いた場合において
も、該h−BN成形体にc−BN化触媒を含浸させた
際、局部的に含浸できない部位が生じたり、また、厚肉
のh−BN成形体を用いた場合、その中心部まではc−
BN化触媒を含浸できない等の問題があること知見し
た。また、上記特公昭60−28782号公報に記載さ
れているように、h−BN成形体を予め窒素ガス中で2
100℃の温度に2時間以上仮焼して酸素含有量を0.
3重量%以下とした場合、h−BNの結晶粒子が成長
し、このため更に含浸性が低下するという問題もあるこ
とを知見した。
However, the present inventor has
In the manufactured h-BN compact, h-BN particles are
They are intimately joined at the contact part, and B 2O3Etc.
The more oxides are present on the surface of the raw material powder, the stronger the bond strength.
Therefore, the density is 1.8 and the porosity is high.
g / cm3When using the following low density compacts
Also, the h-BN compact was impregnated with a c-BN-forming catalyst.
In this case, there are some parts that cannot be impregnated locally,
In the case of using the h-BN molded body of No. 2, c-
We found that there are problems such as impregnation with BN catalyst.
It was Further, it is described in the above Japanese Patent Publication No. 60-28782.
As described above, the h-BN compact was preliminarily subjected to 2 in nitrogen gas.
It is calcined at a temperature of 100 ° C. for 2 hours or more to reduce the oxygen content to 0.
When it is less than 3% by weight, h-BN crystal grains grow.
However, there is also a problem that impregnation is further reduced due to this.
I found out.

【0007】従って、厚肉の六方晶窒化ホウ素(h−B
N)成形体を使用した場合においても、その中心部に至
るまで均一に立方晶窒化ホウ素化触媒(c−BN触媒)
を含浸し得、このため低温低圧条件下においても立方晶
窒化ホウ素(c−BN)焼結体を高純度、高硬度で歩留
まり良く製造することができる成形体が望まれていた。
Therefore, thick-walled hexagonal boron nitride (hB
N) A cubic boron nitride catalyst (c-BN catalyst) is evenly distributed up to the center even when a molded body is used.
Therefore, there has been a demand for a compact capable of producing a cubic boron nitride (c-BN) sintered body with high purity and high hardness at a high yield even under low temperature and low pressure conditions.

【0008】[0008]

【課題を解決するための手段及び作用】本発明者らは上
記要望に応えるため鋭意検討を行った結果、h−BN成
形体に対するc−BN化触媒の含浸性がh−BN成形体
の通気率と相関関係を有し、通気率が0.01cm2
secより小さいh−BN成形体は、その空隙率が高く
ても触媒含浸性が低く、触媒の含浸がせいぜい表面から
0.5mm程度の深さまでしか到達しない(従って、上
述したホットプレス法によるh−BN成形体は低密度で
空隙率が高い場合でも通気率が小さいため触媒含浸性が
悪いものである)ことを見い出すと共に、このように通
気率が低いと、h−BN成形体の表層部においても局部
的に含浸量のバラツキが見られることを見い出した。
Means and Actions for Solving the Problems As a result of intensive investigations by the present inventors in order to meet the above-mentioned demands, as a result, the impregnating property of the c-BN-forming catalyst to the h-BN molded body is determined by the ventilation of the h-BN molded body. The air permeability is 0.01 cm 2 /
The h-BN compact having a size smaller than sec has a low catalyst impregnation property even if its porosity is high, and impregnation of the catalyst reaches a depth of about 0.5 mm from the surface at most (hence, the h by the hot pressing method described above). -BN compacts have poor catalyst impregnation due to low air permeability even when they have low density and high porosity), and when the air permeability is such low, the surface layer part of h-BN compacts It was also found that the dispersion of the impregnated amount was locally observed in the case of.

【0009】これに対しh−BN成形体の通気率が0.
01〜0.3cm2/secの範囲とした場合、c−B
N触媒の含浸性が顕著に増大し、c−BN触媒を拡散含
浸させた場合、h−BN成形体が厚肉(1mm以上)で
あってもその中心部まで触媒の含浸が均一に進行し、触
媒含浸不良による歩留まりの低下や表面と内部との触媒
含浸量のバラツキを防止、低減することができ、これに
よりc−BN焼結体も高品質に歩留まりよく製造できる
ことを知見し、本発明をなすに至った。
On the other hand, the air permeability of the h-BN molded body is 0.
When the range is 01 to 0.3 cm 2 / sec, c−B
When the N-catalyst impregnability is remarkably increased and the c-BN catalyst is diffused and impregnated, even if the h-BN compact has a thick wall (1 mm or more), the impregnation of the catalyst uniformly proceeds up to its central portion. According to the present invention, it has been found that it is possible to prevent or reduce a decrease in yield due to poor catalyst impregnation and a variation in the amount of catalyst impregnated between the surface and the inside, whereby a c-BN sintered body can also be manufactured with high quality and high yield. Came to make.

【0010】従って、本発明は、通気率が0.01〜
0.3cm2/secの六方晶窒化ホウ素成形体に立方
晶窒化ホウ素化触媒を含浸してなることを特徴とする立
方晶窒化ホウ素焼結体製造用成形体を提供する。
Therefore, according to the present invention, the air permeability is 0.01 to.
Provided is a molded product for producing a cubic boron nitride sintered body, which is obtained by impregnating a hexagonal boron nitride molded product of 0.3 cm 2 / sec with a cubic boron nitride conversion catalyst.

【0011】以下、本発明につき更に詳しく説明する
と、本発明のc−BN焼結体製造用の成形体は、h−B
N成形体にc−BN触媒を均一に含浸させてなるもので
ある。
The present invention will be described in more detail below. The molded body for producing a c-BN sintered body of the present invention is h-B.
It is obtained by uniformly impregnating an N molded body with a c-BN catalyst.

【0012】ここで、本発明においては、h−BN成形
体としては、通気率が0.01〜0.3cm2/se
c、好ましくは0.05〜0.2cm2/secである
ものを用いるもので、この範囲の通気率のh−BN成形
体を用いることにより、h−BN成形体が厚さ1mm以
上、特に1〜5mmのものであってもその内部全体にc
−BN化触媒が均等に拡散、含浸されるものである。こ
の場合、通気率が0.01cm2/sec未満の場合、
c−BN化触媒はh−BN成形体の表面から0.5mm
程度の深さまでしか到達せず、またh−BN成形体の表
層部においても局部的に含浸量のバラツキが生じ、本発
明の目的を達成し得ない。また、通気率が0.3cm2
/secを超えるとh−BN成形体の機械的強度が弱く
なるため、取扱いが困難となり、好ましくない。
Here, in the present invention, the h-BN molded product has an air permeability of 0.01 to 0.3 cm 2 / se.
c, preferably 0.05 to 0.2 cm 2 / sec, and by using an h-BN molded product having an air permeability in this range, the h-BN molded product has a thickness of 1 mm or more, Even if it is 1 to 5 mm, it is c
-BN catalyst is uniformly diffused and impregnated. In this case, if the air permeability is less than 0.01 cm 2 / sec,
The c-BN catalyst is 0.5 mm from the surface of the h-BN compact
It reaches only a certain depth, and the impregnated amount locally varies in the surface layer portion of the h-BN compact, so that the object of the present invention cannot be achieved. Also, the air permeability is 0.3 cm 2.
If it exceeds / sec, the mechanical strength of the h-BN compact will be weakened, making handling difficult, which is not preferable.

【0013】なお、本発明において、通気率の値は、直
径20mm,厚さ5mmのh−BN成形体を試験片と
し、図1の装置にて測定した値を下記式(1)に代入し
て求めた値である。
In the present invention, the value of the air permeability is obtained by substituting the value measured by the apparatus of FIG. 1 into the following formula (1) using a h-BN compact having a diameter of 20 mm and a thickness of 5 mm as a test piece. It is the value obtained by

【0014】ここで、図1において、1は試験気体(窒
素ガス)ボンベ、2は試験気体供給器、3は圧力計、4
は試験片、5はパッキン、6は試験片ホルダー、7は流
量計であり、試験片ホルダー6内にパッキン5を介して
厚さ方向が該ホルダー6内に流入する試験気体と対向す
るように取り付けた試験片4に試験気体を通過させ、下
記式(1)から通気率を求めるものである。
Here, in FIG. 1, 1 is a test gas (nitrogen gas) cylinder, 2 is a test gas feeder, 3 is a pressure gauge, 4
Is a test piece, 5 is a packing, 6 is a test piece holder, and 7 is a flow meter, so that the thickness direction in the test piece holder 6 faces the test gas flowing into the holder 6 through the packing 5. A test gas is passed through the attached test piece 4, and the air permeability is obtained from the following formula (1).

【0015】[0015]

【数1】 [Equation 1]

【0016】このような通気率が0.01〜0.3cm
2/secであるh−BN成形体を得る方法としては、
高純度h−BN粉末を200〜10000kg/c
2、より好ましくは1000〜5000kg/cm2
圧力下で静水圧加圧した後、不活性ガス(例えば窒素、
アルゴン等)雰囲気中において1500〜2100℃、
より好ましくは1700〜2000℃の温度で常圧焼成
する方法が推奨される。
Such an air permeability is 0.01 to 0.3 cm
As a method of obtaining an h-BN molded body having 2 / sec,
High-purity h-BN powder 200-10,000 kg / c
m 2 and more preferably after applying hydrostatic pressure under a pressure of 1000 to 5000 kg / cm 2 , an inert gas (for example, nitrogen,
1500 to 2100 ° C. in an atmosphere such as argon,
More preferably, a method of firing at atmospheric pressure at a temperature of 1700 to 2000 ° C. is recommended.

【0017】この場合、上記h−BN粉末はその水分含
有量を乾燥等により1重量%以下に調整したものを用い
ることが必要であり、h−BN粉末の水分含有量が1重
量%を超えると静水圧加圧時に粒子同士の接着力が強ま
り、このため除圧時に成形体に割れが入ったり、あるい
は成形体の通気孔が減少し、焼成後の成形体において通
気率が低くなってしまうなどの問題が発生し易い。
In this case, it is necessary to use the h-BN powder whose water content is adjusted to 1% by weight or less by drying or the like, and the water content of the h-BN powder exceeds 1% by weight. When the hydrostatic pressure is applied, the adhesive force between the particles becomes stronger, which causes cracks in the molded body during depressurization, or the number of ventilation holes in the molded body decreases, resulting in low air permeability in the molded body after firing. Such problems easily occur.

【0018】また、このh−BN粉末の加圧程度、焼成
温度及び時間は以上の通りであるが、得られたh−BN
成形体は上記通気率を有すると共に、その密度が1.5
〜2g/cm3、特に1.6〜1.9g/cm3であるこ
とが、良好なc−BN焼結体を得る点から好ましい。
The pressing degree, firing temperature and time of the h-BN powder are as described above.
The molded body has the above-mentioned air permeability and its density is 1.5.
˜2 g / cm 3 , particularly 1.6 to 1.9 g / cm 3 is preferable from the viewpoint of obtaining a good c-BN sintered body.

【0019】上記h−BN成形体は、これにc−BN化
触媒が含浸される。このh−BN成形体に含浸されるc
−BN化触媒としては、M324やM32(但し、M
はMg,Ca等のアルカリ土類金属を示す)を用いるこ
とが好ましい。
The h-BN compact is impregnated with a c-BN catalyst. C impregnated in this h-BN compact
As the BN-forming catalyst, M 3 B 2 N 4 and M 3 N 2 (however, M
Is an alkaline earth metal such as Mg or Ca).

【0020】h−BN成形体にc−BN化触媒を含浸さ
せる方法としては、上記c−BN化触媒中にh−BN成
形体を埋設し、窒素ガス等の不活性ガス雰囲気中で温度
1000〜1500℃、好ましくは1200〜1300
℃で1〜10時間、好ましくは2〜7時間加熱処理する
方法が好適に採用される。
As a method of impregnating the h-BN compact with the c-BN catalyst, the h-BN compact is embedded in the above-mentioned c-BN catalyst and the temperature is set to 1000 at a temperature of an inert gas such as nitrogen gas. ~ 1500 ° C, preferably 1200 ~ 1300
A method of heat treatment at 1 ° C. for 1 to 10 hours, preferably 2 to 7 hours is suitably adopted.

【0021】このようにして得られた本発明のc−BN
化触媒含浸成形体は、公知の方法によりc−BN焼結体
に転換されるが、この場合良好なc−BN焼結体を得る
には温度1200〜1500℃、圧力3〜7GPaの条
件を採用することが好ましい。
The c-BN of the present invention thus obtained
The hydrogenated catalyst-impregnated molded body is converted into a c-BN sintered body by a known method. In this case, in order to obtain a good c-BN sintered body, a temperature of 1200 to 1500 ° C. and a pressure of 3 to 7 GPa are used. It is preferable to adopt.

【0022】[0022]

【実施例】以下、実施例と比較例を示し、本発明を具体
的に説明するが、本発明は下記の実施例に制限されるも
のではない。
EXAMPLES The present invention will be specifically described below by showing Examples and Comparative Examples, but the present invention is not limited to the following Examples.

【0023】[実施例1〜5、比較例1〜3]水分含有
量1.5重量%のh−BN粉末を温度180℃で種々の
乾燥時間で乾燥させ、表1に示す水分含有量の異なる粉
末を作製し、これをゴム型に充填し、表1に示す条件で
静水圧加圧を行って成形体を得た後、窒素ガス雰囲気中
で焼成してh−BN成形体を製造した。この成形体から
直径20mm、厚さ5mmの試料を取り、上述した方法
に従って通気率を測定した。結果を表1に併記する。な
お、水分含有量は赤外線水分計を用いて試料を加熱し、
加熱前後の重量変化から算出した。
Examples 1 to 5 and Comparative Examples 1 to 3 h-BN powder having a water content of 1.5% by weight was dried at a temperature of 180 ° C. for various drying times to obtain the water content shown in Table 1. Different powders were prepared, filled in a rubber mold, and subjected to isostatic pressing under the conditions shown in Table 1 to obtain a molded product, which was then fired in a nitrogen gas atmosphere to manufacture an h-BN molded product. .. A sample having a diameter of 20 mm and a thickness of 5 mm was taken from this molded body, and the air permeability was measured according to the method described above. The results are also shown in Table 1. The water content is measured by heating the sample using an infrared moisture meter.
It was calculated from the weight change before and after heating.

【0024】次に、これらの試料をMg32中に埋設
し、窒素雰囲気下において1200℃、2時間の加熱処
理を行い、触媒を含浸させた。触媒含浸後の試料断面を
目視及びEPMAにより調べ、含浸性を評価した。この
場合、内部まで均一に含浸されていた場合を良好、局部
的に含浸されていなかったり、表面と中心部のMgの濃
度差が2倍以上であったものを含浸性不良と判定した。
結果を表1に併記する。
Next, these samples were embedded in Mg 3 N 2 and heat-treated at 1200 ° C. for 2 hours in a nitrogen atmosphere to impregnate the catalyst. The cross section of the sample after the catalyst impregnation was examined visually and by EPMA to evaluate the impregnation property. In this case, the case where the inside was uniformly impregnated was good, and the case where the impregnation was not locally performed or the difference in Mg concentration between the surface and the central portion was twice or more was determined to be poor impregnability.
The results are also shown in Table 1.

【0025】[0025]

【表1】 [Table 1]

【0026】表1の結果から明らかなように、本発明に
係るh−BN成形体は触媒含浸性が良好であった。一
方、比較例1の場合、通気率は非常に良好であったが強
度が弱く、取扱いに問題が生じた。比較例2,3は原料
粉末の水分含有量が高いため通気率が低く、h−BN成
形体の表層しか含浸されず、触媒含浸性が不良であっ
た。
As is clear from the results shown in Table 1, the h-BN compact according to the present invention had a good catalyst impregnation property. On the other hand, in the case of Comparative Example 1, the air permeability was very good, but the strength was weak, and there was a problem in handling. In Comparative Examples 2 and 3, since the raw material powder had a high water content, the air permeability was low, only the surface layer of the h-BN compact was impregnated, and the catalyst impregnation property was poor.

【0027】[0027]

【発明の効果】本発明によれば、h−BN成形体へのc
−BN化触媒含浸が容易かつ均一になり、h−BN成形
体が厚肉である場合でも中心部まで安定して均一良好に
触媒が含浸する。このため、厚肉のc−BN焼結体を高
品質に歩留まりよく製造することができる。
According to the present invention, c to h-BN compacts is obtained.
-The BN-ized catalyst is easily and uniformly impregnated, and even when the h-BN compact is thick, the catalyst is stably and uniformly impregnated to the center. Therefore, a thick c-BN sintered body can be manufactured with high quality and high yield.

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

【図1】本発明における通気率を測定するための装置を
示す概略図である。
FIG. 1 is a schematic view showing an apparatus for measuring air permeability in the present invention.

【符号の説明】[Explanation of symbols]

1 試験気体(窒素ガス) 2 試験気体供給器 3 圧力計 4 試験片 5 パッキン 6 試験片ホルダー 7 流量計 1 Test gas (nitrogen gas) 2 Test gas supply device 3 Pressure gauge 4 Test piece 5 Packing 6 Test piece holder 7 Flow meter

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B28B 3/00 102 9261−4G C01B 21/064 M (72)発明者 樫田 周 群馬県安中市磯部2丁目13番1号 信越化 学工業株式会社精密機能材料研究所内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical display location B28B 3/00 102 9261-4G C01B 21/064 M (72) Inventor Shu Kashida Gunma Prefecture Annaka 2-13-1, Isobe, Ichi Shin-Etsu Chemical Co., Ltd. Precision Materials Research Laboratory

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 通気率が0.01〜0.3cm2/se
cの六方晶窒化ホウ素成形体に立方晶窒化ホウ素化触媒
を含浸してなることを特徴とする立方晶窒化ホウ素焼結
体製造用成形体。
1. An air permeability of 0.01 to 0.3 cm 2 / se.
A molded body for producing a cubic boron nitride sintered body, which is obtained by impregnating a hexagonal boron nitride molded body of c with a cubic boron nitride forming catalyst.
JP4080403A 1992-03-02 1992-03-02 Method for producing molded body for producing cubic boron nitride sintered body Expired - Fee Related JP2715794B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4080403A JP2715794B2 (en) 1992-03-02 1992-03-02 Method for producing molded body for producing cubic boron nitride sintered body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4080403A JP2715794B2 (en) 1992-03-02 1992-03-02 Method for producing molded body for producing cubic boron nitride sintered body

Publications (2)

Publication Number Publication Date
JPH05246765A true JPH05246765A (en) 1993-09-24
JP2715794B2 JP2715794B2 (en) 1998-02-18

Family

ID=13717330

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2715794B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005145737A (en) * 2003-11-12 2005-06-09 Denki Kagaku Kogyo Kk Hexagonal boron nitride molded body, production method and use thereof
CN103924288A (en) * 2014-04-01 2014-07-16 许斌 Method for preparing cubic boron nitride monocrystal micro powder by using magnesium-based compound catalyst and application of cubic boron nitride monocrystal micro powder

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60200864A (en) * 1984-03-22 1985-10-11 東芝タンガロイ株式会社 Manufacture of sintered body containing cubic boron nitride
JPS6345175A (en) * 1986-04-09 1988-02-26 住友電気工業株式会社 Method for producing cubic boron nitride sintered body

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60200864A (en) * 1984-03-22 1985-10-11 東芝タンガロイ株式会社 Manufacture of sintered body containing cubic boron nitride
JPS6345175A (en) * 1986-04-09 1988-02-26 住友電気工業株式会社 Method for producing cubic boron nitride sintered body

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005145737A (en) * 2003-11-12 2005-06-09 Denki Kagaku Kogyo Kk Hexagonal boron nitride molded body, production method and use thereof
CN103924288A (en) * 2014-04-01 2014-07-16 许斌 Method for preparing cubic boron nitride monocrystal micro powder by using magnesium-based compound catalyst and application of cubic boron nitride monocrystal micro powder
CN103924288B (en) * 2014-04-01 2016-08-17 山东建筑大学 Use the cubic boron nitride monocrystal micropowder preparation method and application of magnesio composite catalyst

Also Published As

Publication number Publication date
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