JPH08217424A - Hexagonal boron nitride powder and its production - Google Patents

Hexagonal boron nitride powder and its production

Info

Publication number
JPH08217424A
JPH08217424A JP7022830A JP2283095A JPH08217424A JP H08217424 A JPH08217424 A JP H08217424A JP 7022830 A JP7022830 A JP 7022830A JP 2283095 A JP2283095 A JP 2283095A JP H08217424 A JPH08217424 A JP H08217424A
Authority
JP
Japan
Prior art keywords
powder
hbn
nitrogen gas
raw material
nitrogen
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
JP7022830A
Other languages
Japanese (ja)
Other versions
JP3644713B2 (en
Inventor
Taku Kawasaki
卓 川崎
Katsuyasu Nagahama
勝保 長濱
Yukio Kuroda
幸雄 黒田
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.)
Denka Co Ltd
Original Assignee
Denki Kagaku Kogyo KK
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 Denki Kagaku Kogyo KK filed Critical Denki Kagaku Kogyo KK
Priority to JP02283095A priority Critical patent/JP3644713B2/en
Publication of JPH08217424A publication Critical patent/JPH08217424A/en
Application granted granted Critical
Publication of JP3644713B2 publication Critical patent/JP3644713B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Ceramic Products (AREA)

Abstract

PURPOSE: To obtain low-crystalline and highly purified hexagonal boron nitride (hBN) powder. CONSTITUTION: This hexagonal boron nitride powder has >=5 graphitized index (GI-value) by a powder X-ray diffraction method and contains <=1.0wt.% oxygen. In producing this powder by heating and holding a raw material mixture of a boron source compound containing boron and oxygen and a nitrogen source compound containing nitrogen and/or a reducing agent at >=1600 deg.C in a nitrogen gas atmosphere, the reaction is performed in such a state that a nitrogen gas in a supplying ratio of 1-200L/min in a normal state to 1kg of the raw material mixture and/or a gas generating a nitrogen gas at the above-mentioned temperature is circulated so as to be brought into contact with the raw material mixture.

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、六方晶窒化ほう素(h
BN)粉末特に低結晶性かつ高純度のhBN粉末及びそ
の製造方法に関する。
BACKGROUND OF THE INVENTION The present invention relates to hexagonal boron nitride (h
BN) powder, in particular hBN powder with low crystallinity and high purity, and a method for producing the same.

【0002】[0002]

【従来の技術】hBN粉末は、黒鉛と同様の層状構造を
有し、熱伝導性、絶縁性、化学的安定性、固体潤滑性、
耐熱衝撃性などの特性に優れていることから、固体潤滑
・離型剤、樹脂やゴムの充填材、耐熱性・絶縁性焼結体
などに応用されている。
2. Description of the Related Art hBN powder has a layered structure similar to that of graphite, and has thermal conductivity, insulation, chemical stability, solid lubricity,
Due to its excellent properties such as thermal shock resistance, it has been applied to solid lubricants / release agents, fillers of resins and rubbers, heat resistant / insulating sintered bodies, etc.

【0003】hBN粉末の製造法の一例としては以下が
ある。 (1)ほう酸、酸化ほう素又はほう砂などのほう素と酸
素を含むほう素源化合物をリン酸カルシウムなどの充填
材に担持させてからアンモニア雰囲気下で焼成する方
法。 (2)上記ほう素源化合物とジシアンジアミド、メラミ
ン又は尿素などの窒素を含む窒素源化合物との混合物を
焼成する方法。 (3)上記ほう素源化合物と炭素、マグネシウムなどの
還元剤との混合物を窒素ガス雰囲気下で焼成する方法。
The following is an example of a method for producing hBN powder. (1) A method in which a boron source compound containing boron and oxygen such as boric acid, boron oxide or borax is supported on a filler such as calcium phosphate and then baked in an ammonia atmosphere. (2) A method of firing a mixture of the above boron source compound and a nitrogen source compound containing nitrogen such as dicyandiamide, melamine or urea. (3) A method of firing a mixture of the boron source compound and a reducing agent such as carbon or magnesium in a nitrogen gas atmosphere.

【0004】上記のいづれの方法においても、得られる
hBN粉末の結晶性、純度などの特性は、焼成条件特に
焼成温度に大きく依存する。特に1600℃以上におい
ては焼成温度の増大に伴い結晶性の指標となる黒鉛化指
数(GI値)と純度の指標となる酸素量が減少し、結晶
性や純度が著しく向上する。
In any of the above methods, the properties such as crystallinity and purity of the obtained hBN powder greatly depend on the firing conditions, especially the firing temperature. Particularly, at 1600 ° C. or higher, the graphitization index (GI value), which is an index of crystallinity, and the amount of oxygen, which is an index of purity, are decreased with an increase in firing temperature, and the crystallinity and purity are significantly improved.

【0005】黒鉛化指数とは、hBN粉末のX線回折図
に現れる3本の回折ピーク、(100)、(101)、
(102)のピーク面積から(1)式により算出される
値であり、hBNの結晶性が向上するに従いその値は小
さくなり、完全に結晶化したhBNではGI=1.60
になる(J.Thomas et al.,J.Chem.Soc.,84,24,4619-462
2(1963) 参照)。 GI=ピーク面積〔(100) +(101) 〕/ピーク面積(102) ・・・(1)
The graphitization index means three diffraction peaks appearing in the X-ray diffraction pattern of hBN powder, (100), (101),
It is a value calculated from the peak area of (102) by the formula (1), and the value becomes smaller as the crystallinity of hBN is improved, and GI = 1.60 for completely crystallized hBN.
(J.Thomas et al., J.Chem.Soc., 84,24,4619-462
2 (1963)). GI = peak area [(100) + (101)] / peak area (102) (1)

【0006】一方、hBN粉末の酸素量は、通常、低結
晶性(GI値=大)のhBN粉末ほど酸素量が多く、高
結晶性(GI値=小)のhBN粉末ほど酸素量が少な
い。この原因としては、上記ほう素源化合物を原料とす
るhBN粉末の製造においては、ほう素源化合物からの
脱酸素とほう素原子への窒素の結合が連続的に起こるこ
とによるためと考えられる。従って、結晶構造の形成の
不完全な低結晶性hBN粉末の場合、ほう素源化合物か
らの脱酸素も完全ではないので酸素量の多い低純度のh
BN粉末となる。逆に、高結晶性hBN粉末の場合はほ
う素源化合物からの脱酸素が完全に近いため酸素量の少
ない高純度のhBN粉末となる。
On the other hand, the oxygen content of the hBN powder is usually larger in the low crystallinity (GI value = large) hBN powder, and smaller in the high crystallinity (GI value = small) hBN powder. It is considered that this is because the deoxygenation from the boron source compound and the bonding of nitrogen to the boron atom occur continuously in the production of the hBN powder using the boron source compound as a raw material. Therefore, in the case of a low crystalline hBN powder in which the crystal structure is incompletely formed, deoxidation from the boron source compound is not complete, so that a low purity hBN powder containing a large amount of oxygen is used.
It becomes BN powder. On the contrary, in the case of the highly crystalline hBN powder, deoxidation from the boron source compound is almost complete, so that the hBN powder of high purity has a small amount of oxygen.

【0007】通常の高結晶性hBN粉末は、GI値が5
未満で酸素量が1.0重量%未満である。このような高
結晶性かつ高純度のhBN粉末は、固体潤滑・離型剤、
樹脂やゴムの充填材などの用途においては優れた特性を
示すが、hBN焼結体用原料又はhBNを含む複合焼結
体用原料としては焼結体強度が充分でなくなり、また低
結晶性かつ低純度のhBN粉末では焼結体密度が充分で
ないという問題があった。
[0007] Ordinary highly crystalline hBN powder has a GI value of 5
And the amount of oxygen is less than 1.0% by weight. Such highly crystalline and highly pure hBN powder is a solid lubricant / release agent,
It exhibits excellent properties in applications such as resin and rubber fillers, but as a raw material for hBN sintered compacts or a raw material for composite sintered compacts containing hBN, the strength of the sintered compact becomes insufficient, and low crystallinity The low-purity hBN powder has a problem that the density of the sintered body is not sufficient.

【0008】この原因としては、焼結体用原料として高
結晶性かつ高純度のhBN粉末を用いた場合、原料の段
階ですでに結晶化が充分に進んでおり焼結時の原子再配
列は殆ど起こらないので焼結時の物質移動が緩慢とな
り、焼結体内部のhBN粒子間に強固な結合が生じ難く
なって強度が伸びなくなることが考えられる。一方、低
結晶性かつ低純度のhBN粉末を用いた場合はこのよう
な強度発現の問題は少なくなるが、酸素量が多いために
焼結時に酸化ほう素(B2 3 )の液相が生じhBNの
粒成長が起こりやすくなる。hBNは元来異方性の大き
い物質であり、粒子の成長方向にも異方性があるので粒
成長が起こると焼結体内に隙間が生じやすくなり焼結体
の密度が低下してしまうことが考えられる。
The reason for this is that when highly crystalline and highly pure hBN powder is used as the raw material for the sintered body, crystallization has already progressed sufficiently at the stage of the raw material and the atomic rearrangement during sintering is Since it hardly occurs, the mass transfer at the time of sintering becomes slow, and it is conceivable that a strong bond is less likely to occur between the hBN particles inside the sintered body and the strength does not increase. On the other hand, when hBN powder of low crystallinity and low purity is used, such a problem of strength development is reduced, but since the amount of oxygen is large, a liquid phase of boron oxide (B 2 O 3 ) is generated during sintering. The resulting hBN grains are likely to grow. Since hBN is a substance with a large anisotropy by nature, and since the grain growth direction is also anisotropic, when grain growth occurs, gaps are likely to occur in the sintered body and the density of the sintered body will decrease. Can be considered.

【0009】[0009]

【発明が解決しようとする課題】本発明は、以上の状況
に鑑みなされたものであって、高密度かつ高強度のhB
N焼結体又はhBNを含む複合焼結体を製造することの
できるhBN粉末とその製造方法を提供することを目的
とするものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the above situation, and has a high density and high strength hB.
It is an object of the present invention to provide an hBN powder capable of producing an N sintered body or a composite sintered body containing hBN and a method for producing the same.

【0010】[0010]

【課題を解決するための手段】すなわち、本発明は、粉
末X線回折法における黒鉛化指数(GI値)が5以上で
あり、かつ酸素量が1.0重量%以下であることを特徴
をする六方晶窒化ほう素粉末、及びほう素と酸素を含む
ほう素源化合物と、窒素を含む窒素源化合物及び/又は
還元剤とからなる原料混合物を窒素ガス雰囲気下160
0℃以上の温度で加熱保持して六方晶窒化ほう素粉末を
製造する方法において、上記窒素ガス雰囲気は、原料混
合物1kgに対して標準状態で1〜200リットル/分
の窒素ガス及び/又は上記温度で窒素ガスを生成するガ
スを原料混合物に直接接触させるように流通させて形成
させたものであることを特徴とする六方晶窒化ほう素粉
末の製造方法である。
That is, the present invention is characterized in that the graphitization index (GI value) in the powder X-ray diffraction method is 5 or more and the amount of oxygen is 1.0% by weight or less. A hexagonal boron nitride powder, a raw material mixture containing a boron source compound containing boron and oxygen, and a nitrogen source compound containing nitrogen and / or a reducing agent under a nitrogen gas atmosphere.
In the method for producing a hexagonal boron nitride powder by heating and holding at a temperature of 0 ° C. or higher, the nitrogen gas atmosphere is 1 to 200 liter / min of nitrogen gas in a standard state with respect to 1 kg of the raw material mixture and / or the above. The method for producing a hexagonal boron nitride powder is characterized in that the hexagonal boron nitride powder is formed by circulating a gas that produces nitrogen gas at a temperature so as to directly contact the raw material mixture.

【0011】以下、さらに詳しく本発明を説明すると、
本発明のhBN粉末は、GI値が5以上で酸素量が1.
0重量%以下好ましくは0.5重量%以下である低結晶
性かつ高純度のhBN粉末である。本発明のhBN粉末
は、従来のものが高結晶性かつ高純度、低結晶性かつ低
純度、又は高結晶性かつ低純度のいずれかであったもの
と比較して異なっている。この理由は、前二者について
は、上記のように通常の製造法によるhBN粉末の酸素
量は結晶性に依存して変化するためであり、また後者に
ついては、高結晶性hBN粉末を製造した後の精製が不
十分であるか又は意図的に酸素を含む物質が添加された
ためである。
The present invention will be described in more detail below.
The hBN powder of the present invention has a GI value of 5 or more and an oxygen content of 1.
The hBN powder has a low crystallinity and a high purity of 0% by weight or less, preferably 0.5% by weight or less. The hBN powder of the present invention is different from the conventional ones which are either highly crystalline and highly pure, low crystalline and low pure, or highly crystalline and low pure. The reason for this is that in the former two cases, the oxygen content of the hBN powder by the usual production method changes depending on the crystallinity as described above, and in the latter case, a highly crystalline hBN powder was produced. This is because the subsequent purification is insufficient or a substance containing oxygen is intentionally added.

【0012】本発明において、GI値が5未満又は酸素
量が1.0重量%をこえると、高密度かつ高強度のhB
N焼結体又はhBNを含む複合焼結体を製造することが
できない。本発明のhBN粉末は、低結晶性であるため
に焼結体内部の粒子間に強固な結合を形成し、また高純
度であるために焼結体内部における粒成長を抑制するこ
とができる。
In the present invention, when the GI value is less than 5 or the oxygen content exceeds 1.0% by weight, hB of high density and high strength is obtained.
It is not possible to manufacture an N sintered body or a composite sintered body containing hBN. Since the hBN powder of the present invention has low crystallinity, a strong bond is formed between particles inside the sintered body, and since it is highly pure, grain growth inside the sintered body can be suppressed.

【0013】次に、本発明のhBN粉末の製造方法につ
いて説明する。本発明の大きな特徴は、原料混合物を温
度1600℃以上の窒素雰囲気下で保持する際に、原料
混合物1kgに対して標準状態で1〜200リットル/
分の窒素ガス及び/又は1600℃以上の温度で窒素ガ
スを生成するガスを流通させること、及びその窒素ガス
及び/又は窒素ガスを生成するガス流を原料混合物に直
接接触させることである。
Next, a method for producing the hBN powder of the present invention will be described. A major feature of the present invention is that when the raw material mixture is held in a nitrogen atmosphere at a temperature of 1600 ° C. or higher, it is 1 to 200 liters / liter in a standard state for 1 kg of the raw material mixture.
A minute nitrogen gas and / or a gas that produces nitrogen gas at a temperature of 1600 ° C. or higher is passed, and the nitrogen gas and / or a gas stream that produces nitrogen gas is brought into direct contact with the raw material mixture.

【0014】本発明における窒素ガス流及び/又は窒素
ガスを生成するガス流の作用は、hBN粉末の結晶性を
向上させることなくhBN粉末中に含まれる酸素を除去
すること、及びhBNの分解を抑制することであり、こ
れによって低結晶性かつ高純度でしかも粒成長の抑制さ
れたBET比表面積10m2 /g以上の微細なhBN粉
末を製造することができる。1600℃以上の温度で窒
素ガスを生成するガスとしてはアンモニアガス等をあげ
ることができる。
The effect of the nitrogen gas stream and / or the gas stream that produces nitrogen gas in the present invention is to remove oxygen contained in the hBN powder without improving the crystallinity of the hBN powder, and to decompose hBN. By this, it is possible to produce a fine hBN powder having a BET specific surface area of 10 m 2 / g or more, which has low crystallinity, high purity, and suppressed grain growth. As a gas that produces nitrogen gas at a temperature of 1600 ° C. or higher, ammonia gas or the like can be used.

【0015】アルゴンなどの不活性ガスや水素ガスなど
は、1600℃未満の温度で使用できるが、それ以上の
温度ではhBNの分解を抑制する作用を有しないので本
発明には適さない。
Although an inert gas such as argon or hydrogen gas can be used at a temperature lower than 1600 ° C., it is not suitable for the present invention at a temperature higher than that, since it has no effect of suppressing the decomposition of hBN.

【0016】本発明における窒素ガス及び/又は窒素ガ
スを生成するガスは流通させることが必要である。これ
はこれらのガスを静置させるとhBN粉末から揮発した
酸素を含むガスが気相中で飽和してそれ以後の揮発が進
行し難くなるためである。
In the present invention, the nitrogen gas and / or the gas that produces the nitrogen gas must be circulated. This is because when these gases are allowed to stand, the gas containing oxygen volatilized from the hBN powder is saturated in the gas phase and the volatilization thereafter becomes difficult to proceed.

【0017】また、本発明においては、窒素ガス流及び
/又は窒素ガスを生成するガス流は原料混合物に直接接
触させることが必要である。これを怠るとこれらのガス
に接触しない部位におけるhBN粉末からの脱酸素が円
滑に進行しない。
Further, in the present invention, it is necessary that the nitrogen gas stream and / or the gas stream for producing nitrogen gas be brought into direct contact with the raw material mixture. If this is neglected, the deoxidation from the hBN powder in the parts that do not come into contact with these gases does not proceed smoothly.

【0018】窒素ガス流及び/又は窒素ガスを生成する
ガス流を原料混合物に直接接触させる方法としては、例
えば孔を多数あけた篭状ルツボに原料混合物を充填した
後、ルツボの下部よりこれらのガスを流通させる方法、
原料混合物の充填部にパイプを挿入しこのパイプの先端
又はパイプ側面に設けられた孔からこれらのガスを流出
させる方法などである。
As a method for directly contacting the nitrogen gas stream and / or the gas stream for producing nitrogen gas with the raw material mixture, for example, after filling the raw material mixture into a basket-like crucible having a large number of holes, these crucibles are placed under the crucible. A method of circulating gas,
For example, a method may be used in which a pipe is inserted into the filling portion of the raw material mixture and these gases are caused to flow out through a hole provided at the tip of the pipe or the side surface of the pipe.

【0019】窒素ガス及び/又は窒素ガスを生成するガ
スの流量は、原料混合物1kgに対して標準状態で1〜
200リットル/分好ましくは5〜100リットル/分
である。1リットル/分未満ではhBN粉末からの脱酸
素が充分とはならなず、また200リットル/分をこえ
るとこれらのガスによる持ち去られる熱が大きくなり好
ましくはない。窒素ガス及び/又は窒素ガスを生成する
ガスの流通は1600℃以上の温度で行われる。温度が
これよりも低いと窒素ガス及び/又は窒素ガスを生成す
るガスの流通の有無に関係なくhBN粉末からの脱酸素
が充分に起こらなくなる。
The flow rate of the nitrogen gas and / or the gas for producing the nitrogen gas is 1 to 1 kg in a standard state for 1 kg of the raw material mixture.
200 liters / minute, preferably 5 to 100 liters / minute. If it is less than 1 liter / min, deoxidation from the hBN powder is not sufficient, and if it exceeds 200 liter / min, the heat carried away by these gases becomes large, which is not preferable. The flow of the nitrogen gas and / or the gas that generates the nitrogen gas is performed at a temperature of 1600 ° C. or higher. When the temperature is lower than this, deoxygenation from the hBN powder does not sufficiently occur regardless of whether or not the nitrogen gas and / or the gas that generates the nitrogen gas is passed.

【0020】本発明で使用される原料混合物は、ほう素
と酸素を含むほう素源化合物と、窒素を含む窒素源化合
物及び/又は還元剤との混合物である。これらの配合例
を示せば、ほう素源化合物100重量部に対し、窒素源
化合物及び/又は還元剤10〜200重量部である。
The raw material mixture used in the present invention is a mixture of a boron source compound containing boron and oxygen, and a nitrogen source compound containing nitrogen and / or a reducing agent. If these formulation examples are shown, the nitrogen source compound and / or the reducing agent is 10 to 200 parts by weight with respect to 100 parts by weight of the boron source compound.

【0021】ほう素源化合物としては、例えばほう酸、
酸化ほう素、ほう砂、無水ほう砂などのほう素と酸素を
含む化合物、また窒素源化合物としては、メラミン、ジ
シアンジアミド、尿素などの含窒素有機化合物、更に還
元剤としては、炭素や、マグネシウム、カルシウムなど
の還元性を有する金属などが使用される。
Examples of the boron source compound include boric acid,
Boron oxide, borax, a compound containing boron and oxygen such as anhydrous borax, a nitrogen source compound, melamine, dicyandiamide, a nitrogen-containing organic compound such as urea, further reducing agents, carbon and magnesium, A reducing metal such as calcium is used.

【0022】[0022]

【実施例】以下、実施例及び比較例をあげて更に具体的
に本発明を説明する。
EXAMPLES The present invention will be described more specifically with reference to Examples and Comparative Examples.

【0023】実施例1 ほう酸(H3 BO3 )990グラムとメラミン(C3
6 6 )1010グラムをボールミルで1時間混合した
後、金型を用いて直径20mm、高さ20mmの円柱状
成形体からなる原料混合物を多数個成形した。これら
を、底面に直径10mmの孔が多数設けられた直径30
0mm、高さ300mmの蓋のない熱分解窒化ほう素製
ルツボに充填し、高周波誘導型加熱炉の黒鉛製反応管内
に配置した。
Example 1 990 grams of boric acid (H 3 BO 3 ) and melamine (C 3 N
After 1010 grams of 6 H 6 ) was mixed in a ball mill for 1 hour, a large number of raw material mixtures consisting of cylindrical molded bodies having a diameter of 20 mm and a height of 20 mm were molded using a mold. These have a diameter of 30 mm with a large number of holes of 10 mm in diameter on the bottom.
A crucible made of 0 mm and a height of 300 mm, which had no lid and was made of pyrolytic boron nitride, was filled and placed in a graphite reaction tube of a high-frequency induction heating furnace.

【0024】次に、黒鉛製反応管底部に設けられた窒素
ガス導入孔から、標準状態で1リットル/分(原料混合
物1kg当たり0.5リットル/分)の窒素ガスを供給
した。なお、上記ルツボは、窒素ガスがルツボ内を流通
するように窒素ガス導入孔の開口部がルツボ底部に接す
るように配置されている。
Next, 1 liter / minute (0.5 liter / minute per 1 kg of the raw material mixture) of nitrogen gas was supplied in a standard state from the nitrogen gas introduction hole provided at the bottom of the graphite reaction tube. The crucible is arranged so that the opening of the nitrogen gas introduction hole is in contact with the bottom of the crucible so that the nitrogen gas flows through the crucible.

【0025】原料混合物を15℃/分の速度で加熱・昇
温し、温度が1600℃に達した時点で窒素ガス流量を
2リットル/分(原料混合物1kg当たり1リットル/
分)に増やした。その後、再度15℃/分の速度で20
00℃まで昇温し、その温度で2時間保持してから加熱
を止め室温まで自然冷却した。
The raw material mixture is heated and heated at a rate of 15 ° C./minute, and when the temperature reaches 1600 ° C., the nitrogen gas flow rate is 2 liters / minute (1 liter / kg of the raw material mixture).
Minutes). Then, again at a rate of 15 ° C / min for 20
The temperature was raised to 00 ° C., the temperature was maintained for 2 hours, the heating was stopped, and the temperature was naturally cooled to room temperature.

【0026】得られた生成物は、軽い衝撃を加えること
により容易に粉砕することのできる白色の塊体であっ
た。これをボールミルで約1時間粉砕して約400グラ
ムの白色粉末を得た。これをX線回折分析をしたとこ
ろ、hBNの回折パターンを示しその黒鉛化指数(GI
値)は7.42であった。また、酸素量を堀場製作所製
O/N同時分析装置(EMGA−2800)で測定した
ところ、0.23重量%であった。
The product obtained was a white mass which could be easily ground by applying a light impact. This was ground in a ball mill for about 1 hour to obtain about 400 grams of white powder. When this was subjected to X-ray diffraction analysis, it showed a diffraction pattern of hBN, and its graphitization index (GI
The value) was 7.42. Moreover, when the oxygen amount was measured by an O / N simultaneous analysis apparatus (EMGA-2800) manufactured by Horiba, Ltd., it was 0.23% by weight.

【0027】得られたhBN粉末の焼結性を評価するた
め、直径40mm、高さ60mmの成形体に金型成形
し、それを表1に示す条件で常圧焼結をしたところ、表
1に示されるカサ密度と曲げ強度(JIS R 160
1における3点曲げ試験)を有するhBN焼結体が製造
された。
In order to evaluate the sinterability of the obtained hBN powder, a green body having a diameter of 40 mm and a height of 60 mm was die-molded and pressure-sintered under the conditions shown in Table 1. The bulk density and bending strength shown in (JIS R 160
A hBN sintered body having a three-point bending test in 1) was produced.

【0028】実施例2 実施例1で製造されたhBN粉末に表1に示す添加剤を
内割配合し、実施例1と同様にして金型成形した後、表
1に示す条件で常圧焼結をしたところ、表1に示される
密度と曲げ強度を有するhBN焼結体が製造された。
Example 2 The hBN powder produced in Example 1 was internally compounded with the additives shown in Table 1 and molded by a mold in the same manner as in Example 1 and then baked under normal pressure under the conditions shown in Table 1. Upon binding, an hBN sintered body having the density and bending strength shown in Table 1 was produced.

【0029】実施例3 酸化ほう素560グラム、炭素粉末(アセチレンブラッ
ク)250グラム、水200グラムをヘンシェルミキサ
ーにて20分間混合した後、実施例1と同様に成形して
原料混合物を多数個作製した。これらを、直径300m
m、高さ200mmのhBN焼結体製のルツボに充填し
た。この際、窒素ガス流通用として直径20mm、長さ
300mmのhBN焼結体製パイプを下端の開口部がル
ツボ内壁底面から約15mmの高さに位置するように挿
入した。その後、ルツボを高周波誘導型加熱炉の黒鉛製
反応管内に配置し、更に上記ガス流通用hBN焼結体製
パイプの上端を既設の窒素ガス配管に接続し、標準状態
で10リットル/分の窒素ガスを供給した。
Example 3 560 grams of boron oxide, 250 grams of carbon powder (acetylene black) and 200 grams of water were mixed for 20 minutes in a Henschel mixer, and then molded in the same manner as in Example 1 to prepare a large number of raw material mixtures. did. These are 300m in diameter
It was filled in a crucible made of an hBN sintered body having a height of m and a height of 200 mm. At this time, a pipe made of hBN sintered body having a diameter of 20 mm and a length of 300 mm was inserted so that the opening at the lower end was located at a height of about 15 mm from the bottom surface of the inner wall of the crucible for nitrogen gas flow. After that, the crucible was placed in a graphite reaction tube of a high-frequency induction heating furnace, and the upper end of the hBN sintered pipe for gas distribution was connected to an existing nitrogen gas pipe, and 10 l / min of nitrogen was supplied under standard conditions. Gas was supplied.

【0030】原料混合物を20℃/分の速度で加熱・昇
温し、温度が1800℃に達した時点で昇温を止めその
まま4時間保持した後、室温まで自然冷却した。得られ
た生成物は実施例1同様の白色塊体であり、これを実施
例1と同様に粉砕することによって約300グラムの白
色粉末が得られた。この白色粉末のX線回折分析結果
は、hBNの回折パターンを示し、その黒鉛化指数(G
I値)は9.12であった。また、酸素量は0.42重
量%であった。
The raw material mixture was heated and heated at a rate of 20 ° C./min. When the temperature reached 1800 ° C., the heating was stopped and the temperature was maintained for 4 hours and then naturally cooled to room temperature. The obtained product was a white lump similar to that in Example 1, and this was crushed in the same manner as in Example 1 to obtain about 300 g of a white powder. The X-ray diffraction analysis result of this white powder shows the diffraction pattern of hBN, and its graphitization index (G
The I value) was 9.12. The amount of oxygen was 0.42% by weight.

【0031】上記で製造されたhBN粉末を実施例1と
同様にして金型成形した後、表1に示す条件でホットプ
レス焼結をしたところ、表1に示される密度と曲げ強度
を有するhBN焼結体が製造された。
The hBN powder produced as described above was die-molded in the same manner as in Example 1 and hot-press sintered under the conditions shown in Table 1. As a result, hBN having the density and bending strength shown in Table 1 was obtained. A sintered body was produced.

【0032】実施例4 実施例3で製造されたhBN粉末に表1に示す添加剤を
内割配合し、実施例1と同様にして金型成形した後、表
1に示す条件で常圧焼結をしたところ、表1に示される
密度と曲げ強度を有するhBNを含む複合焼結体が製造
された。
Example 4 The hBN powder produced in Example 3 was internally compounded with the additives shown in Table 1, molded in the same manner as in Example 1, and then baked under normal pressure under the conditions shown in Table 1. Upon binding, a composite sintered body containing hBN having the density and bending strength shown in Table 1 was produced.

【0033】実施例5 無水ほう砂(Na2 4 7 )800グラム、ジシアン
ジアミド(C2 4 4 )1000グラムの混合粉末か
らなる原料混合物を実施例3と同様の通気用パイプを立
てたルツボに充填してから加熱炉内に配置し、標準状態
で2リットル/分のアンモニアガスを供給した。
Example 5 Anhydrous borax (Na2BFourO7) 800 grams, dicyan
Diamide (C2NFourH Four) 1000 grams of mixed powder
The raw material mixture consisting of
After filling in the crucible, place it in the heating furnace and
To supply 2 liter / min of ammonia gas.

【0034】その後、25℃/分の速度で加熱・昇温
し、1900℃の温度で3時間保持した後室温まで自然
冷却し、実施例1と同様に粉砕して約400グラムの白
色粉末を得た。この白色粉末のX線回折分析結果は、h
BNの回折パターンを示し、GI値は6.14であっ
た。また、酸素量は0.66重量%であった。
Then, the mixture was heated and heated at a rate of 25 ° C./minute, kept at a temperature of 1900 ° C. for 3 hours, naturally cooled to room temperature, and pulverized in the same manner as in Example 1 to obtain about 400 g of a white powder. Obtained. The X-ray diffraction analysis result of this white powder is h
The diffraction pattern of BN was shown, and the GI value was 6.14. The amount of oxygen was 0.66% by weight.

【0035】上記で製造されたhBN粉末に表1に示す
添加剤を内割配合し、実施例1と同様にして金型成形し
た後、表1に示す条件で常圧焼結をしたところ、表1に
示される密度と曲げ強度を有するhBN焼結体が製造さ
れた。
The hBN powder produced above was internally blended with the additives shown in Table 1, mold-molded in the same manner as in Example 1, and then pressure-sintered under the conditions shown in Table 1. An hBN sintered body having the density and bending strength shown in Table 1 was produced.

【0036】比較例1 1600℃において窒素ガス流量を増大させなかったこ
と以外は、実施例1と同様にして操作したところ、約5
00グラムの白色粉末が得られた。この粉末のX線回折
分析結果は、hBNの回折パターンを示し、GI値は
2.60であった。また、酸素量は0.15重量%であ
った。
Comparative Example 1 When operated in the same manner as in Example 1 except that the nitrogen gas flow rate was not increased at 1600 ° C., about 5
00 grams of white powder was obtained. The X-ray diffraction analysis result of this powder showed the diffraction pattern of hBN, and the GI value was 2.60. The amount of oxygen was 0.15% by weight.

【0037】上記で製造されたhBN粉末を実施例1と
同様にして金型成形した後、表1に示す条件でホットプ
レス焼結をしたところ、表1に示される密度と曲げ強度
を有するhBN焼結体が製造された。
The hBN powder produced as described above was die-molded in the same manner as in Example 1 and hot-press sintered under the conditions shown in Table 1. As a result, hBN having the density and bending strength shown in Table 1 was obtained. A sintered body was produced.

【0038】比較例2 比較例1で製造されたhBN粉末に表1に示す添加剤を
内割配合し、実施例1と同様にして金型成形した後、表
1に示す条件で常圧焼結をしたところ、表1に示される
密度と曲げ強度を有するhBN焼結体が製造された。
COMPARATIVE EXAMPLE 2 The hBN powder produced in Comparative Example 1 was internally compounded with the additives shown in Table 1, molded in the same manner as in Example 1, and then baked under normal pressure under the conditions shown in Table 1. Upon binding, an hBN sintered body having the density and bending strength shown in Table 1 was produced.

【0039】比較例3 実施例1と同様の原料混合物を、底面に孔の設けられい
ない直径300mm、高さ300mmの蓋のない黒鉛製
ルツボに充填し高周波誘導型加熱炉の黒鉛製反応管内に
配置してから、反応管上部の窒素ガス導入孔からルツボ
内の原料混合物の表層に直接当たるように、標準状態で
3リットル/分(原料混合物1kg当たり1.5リット
ル/分)の窒素ガスを供給した。
Comparative Example 3 The same raw material mixture as in Example 1 was filled in a graphite crucible having a diameter of 300 mm and a height of 300 mm with no holes on the bottom and made of a lid, and placed in a graphite reaction tube of a high-frequency induction heating furnace. After arranging, 3 liter / min (1.5 liter / min per 1 kg of raw material mixture) nitrogen gas in a standard state so as to directly hit the surface layer of the raw material mixture in the crucible through the nitrogen gas introduction hole in the upper part of the reaction tube. Supplied.

【0040】その後、原料混合物を15℃/分の速度で
加熱・昇温し、1500℃の温度で2時間保持した後、
室温まで自然冷却した。
After that, the raw material mixture was heated and heated at a rate of 15 ° C./min and kept at a temperature of 1500 ° C. for 2 hours,
It was naturally cooled to room temperature.

【0041】得られた生成物には、表層部と底部に透明
なガラス状の析出物が認められ、元素分析の結果、酸化
ほう素(B2 3 )であることがわかった。これ以外の
部位は、実施例1と同様の白色の塊体であり、実施例1
と同様に粉砕して420グラムの白色粉末を得た。これ
を硝酸水溶液で処理後水洗・乾燥してB2 3 を除去し
約400グラムの白色粉末を得た。この白色粉末のX線
回折分析結果は、hBNの回折パターンを示し、GI値
は8.08であった。また、酸素量は1.16重量%で
あった。
In the obtained product, transparent glass-like precipitates were found on the surface and bottom, and elemental analysis revealed that it was boron oxide (B 2 O 3 ). The other parts are white lumps similar to those in Example 1.
Trituration in the same manner as above gave 420 grams of white powder. This was treated with an aqueous nitric acid solution, washed with water and dried to remove B 2 O 3 to obtain about 400 g of a white powder. The X-ray diffraction analysis result of this white powder showed the diffraction pattern of hBN, and the GI value was 8.08. The amount of oxygen was 1.16% by weight.

【0042】上記で製造されたhBN粉末を実施例1と
同様にして金型成形した後、表1に示す条件で常圧焼結
をしたところ、表1に示される密度と曲げ強度を有する
hBN焼結体が製造された。
The hBN powder produced above was molded in the same manner as in Example 1 and thereafter pressure-sintered under the conditions shown in Table 1. As a result, hBN having the density and bending strength shown in Table 1 was obtained. A sintered body was produced.

【0043】比較例4 比較例3で製造されたhBN粉末に表1に示す添加剤を
内割(確認)配合し、実施例1と同様にして金型成形し
た後、表1に示す条件でホットプレス焼結をしたとこ
ろ、表1に示される密度と曲げ強度を有するhBNを含
む複合焼結体が製造された。
Comparative Example 4 The additives shown in Table 1 were added to the hBN powder produced in Comparative Example 3.
After compounding the inner ratio (confirmation ), molding the mixture in the same manner as in Example 1, and performing hot press sintering under the conditions shown in Table 1, a composite containing hBN having the density and bending strength shown in Table 1 was obtained. A sintered body was produced.

【0044】参考例1 表1に示すGI値と酸素量を有する市販hBN粉末を実
施例1と同様にして金型成形した後、表1に示す条件で
ホットプレス焼結をしたところ、表1に示される密度と
曲げ強度を有するhBN焼結体が製造された。
Reference Example 1 Commercially available hBN powder having a GI value and an oxygen content shown in Table 1 was mold-molded in the same manner as in Example 1 and hot-press sintered under the conditions shown in Table 1. An hBN sintered body having the density and bending strength shown in Table 1 was produced.

【0045】参考例2 表1に示すGI値と酸素量を有する市販hBN粉末に表
1に示す添加剤を内割配合し、実施例1と同様にして金
型成形した後、表1に示す条件でホットプレス焼結をし
たところ、表1に示される密度と曲げ強度を有するhB
Nを含む複合焼結体が製造された。
Reference Example 2 A commercially available hBN powder having a GI value and an oxygen content shown in Table 1 was internally compounded with the additive shown in Table 1 and molded in the same manner as in Example 1, and then shown in Table 1. When hot press sintering under the conditions, hB having the density and bending strength shown in Table 1 is obtained.
A composite sintered body containing N was produced.

【0046】[0046]

【表1】 [Table 1]

【0047】[0047]

【発明の効果】本発明によれば、従来にない低結晶性か
つ高純度のhBN粉末が提供され、高強度かつ高密度の
hBN焼結体又はhBNを含む複合焼結体を製造するこ
とができる。
According to the present invention, an unprecedented low crystallinity and high purity hBN powder is provided, and a high strength and high density hBN sintered body or a composite sintered body containing hBN can be manufactured. it can.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 粉末X線回折法における黒鉛化指数(G
I値)が5以上であり、かつ酸素量が1.0重量%以下
であることを特徴をする六方晶窒化ほう素粉末。
1. A graphitization index (G) in a powder X-ray diffraction method.
A hexagonal boron nitride powder having an I value of 5 or more and an oxygen content of 1.0% by weight or less.
【請求項2】 ほう素と酸素を含むほう素源化合物と、
窒素を含む窒素源化合物及び/又は還元剤とからなる原
料混合物を窒素ガス雰囲気下1600℃以上の温度で加
熱保持して六方晶窒化ほう素粉末を製造する方法におい
て、上記窒素ガス雰囲気は、原料混合物1kgに対して
標準状態で1〜200リットル/分の窒素ガス及び/又
は上記温度で窒素ガスを生成するガスを原料混合物に直
接接触させるように流通させて形成させたものであるこ
とを特徴とする六方晶窒化ほう素粉末の製造方法。
2. A boron source compound containing boron and oxygen,
In the method for producing a hexagonal boron nitride powder by heating and holding a raw material mixture comprising a nitrogen source compound containing nitrogen and / or a reducing agent at a temperature of 1600 ° C. or higher in a nitrogen gas atmosphere, the nitrogen gas atmosphere is a raw material. 1 to 200 liters / min of nitrogen gas in a standard state for 1 kg of a mixture and / or a gas that produces nitrogen gas at the above temperature is circulated so as to be in direct contact with the raw material mixture. And a method for producing a hexagonal boron nitride powder.
JP02283095A 1995-02-10 1995-02-10 Method for producing hexagonal boron nitride powder Expired - Lifetime JP3644713B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02283095A JP3644713B2 (en) 1995-02-10 1995-02-10 Method for producing hexagonal boron nitride powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02283095A JP3644713B2 (en) 1995-02-10 1995-02-10 Method for producing hexagonal boron nitride powder

Publications (2)

Publication Number Publication Date
JPH08217424A true JPH08217424A (en) 1996-08-27
JP3644713B2 JP3644713B2 (en) 2005-05-11

Family

ID=12093621

Family Applications (1)

Application Number Title Priority Date Filing Date
JP02283095A Expired - Lifetime JP3644713B2 (en) 1995-02-10 1995-02-10 Method for producing hexagonal boron nitride powder

Country Status (1)

Country Link
JP (1) JP3644713B2 (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000042823A (en) * 1998-05-26 2000-02-15 Sumitomo Electric Ind Ltd Milling cutter and manufacture thereof
KR100341723B1 (en) * 2000-05-16 2002-06-24 조종목 Process for producing hexagonal Boron Nitride using self-propagating high-temperature synthesis
JP2004250264A (en) * 2003-02-19 2004-09-09 Rikogaku Shinkokai High strength boron nitride sintered compact and method of manufacturing the same
KR100461962B1 (en) * 2002-07-30 2004-12-17 임동수 Process for producing composite powders of metallic oxides/nitride compounds
JP2005336009A (en) * 2004-05-27 2005-12-08 National Institute For Materials Science Silicon nitride nano-wire coated with silicon nitride nano-sheet and its manufacturing method
US7061017B2 (en) 1996-08-19 2006-06-13 Sanyo Electric Co., Ltd. Laser anneal method of a semiconductor layer
JP2007031170A (en) * 2005-07-22 2007-02-08 National Institute For Materials Science Boron nitride-based porous body and its manufacturing method
JP2007051228A (en) * 2005-08-19 2007-03-01 Denki Kagaku Kogyo Kk Engine oil
JP2007217281A (en) * 2007-05-22 2007-08-30 Sumitomo Electric Ind Ltd Cubical boron nitride sintered compact and method of manufacturing the same
JP2008189488A (en) * 2007-02-02 2008-08-21 Denki Kagaku Kogyo Kk Slurry containing boron nitride
JP2015504101A (en) * 2011-12-16 2015-02-05 ティコナ・エルエルシー Boron-containing nucleating agent for polyarylene sulfide

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60260405A (en) * 1984-06-07 1985-12-23 Kawasaki Steel Corp Hexagonal boron nitride powder and its manufacture
JPS6158806A (en) * 1984-08-30 1986-03-26 Kawasaki Steel Corp Manufacture of high-purity hexagonal boron nitride powder
JPS6256308A (en) * 1985-05-10 1987-03-12 Kawasaki Steel Corp Hexagonal boron nitride powder having excellent sintering characteristic

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60260405A (en) * 1984-06-07 1985-12-23 Kawasaki Steel Corp Hexagonal boron nitride powder and its manufacture
JPS6158806A (en) * 1984-08-30 1986-03-26 Kawasaki Steel Corp Manufacture of high-purity hexagonal boron nitride powder
JPS6256308A (en) * 1985-05-10 1987-03-12 Kawasaki Steel Corp Hexagonal boron nitride powder having excellent sintering characteristic

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7439114B2 (en) 1996-08-19 2008-10-21 Sanyo Electric Co., Ltd. Laser anneal method of a semiconductor layer
US7061017B2 (en) 1996-08-19 2006-06-13 Sanyo Electric Co., Ltd. Laser anneal method of a semiconductor layer
JP2000042823A (en) * 1998-05-26 2000-02-15 Sumitomo Electric Ind Ltd Milling cutter and manufacture thereof
KR100341723B1 (en) * 2000-05-16 2002-06-24 조종목 Process for producing hexagonal Boron Nitride using self-propagating high-temperature synthesis
KR100461962B1 (en) * 2002-07-30 2004-12-17 임동수 Process for producing composite powders of metallic oxides/nitride compounds
JP2004250264A (en) * 2003-02-19 2004-09-09 Rikogaku Shinkokai High strength boron nitride sintered compact and method of manufacturing the same
JP4542747B2 (en) * 2003-02-19 2010-09-15 国立大学法人東京工業大学 Manufacturing method of high strength hexagonal boron nitride sintered body
JP2005336009A (en) * 2004-05-27 2005-12-08 National Institute For Materials Science Silicon nitride nano-wire coated with silicon nitride nano-sheet and its manufacturing method
JP4581121B2 (en) * 2004-05-27 2010-11-17 独立行政法人物質・材料研究機構 Silicon nitride nanowire coated with boron nitride nanosheet and method for producing the same
JP2007031170A (en) * 2005-07-22 2007-02-08 National Institute For Materials Science Boron nitride-based porous body and its manufacturing method
JP2007051228A (en) * 2005-08-19 2007-03-01 Denki Kagaku Kogyo Kk Engine oil
JP2008189488A (en) * 2007-02-02 2008-08-21 Denki Kagaku Kogyo Kk Slurry containing boron nitride
JP2007217281A (en) * 2007-05-22 2007-08-30 Sumitomo Electric Ind Ltd Cubical boron nitride sintered compact and method of manufacturing the same
JP2015504101A (en) * 2011-12-16 2015-02-05 ティコナ・エルエルシー Boron-containing nucleating agent for polyarylene sulfide
JP2017141452A (en) * 2011-12-16 2017-08-17 ティコナ・エルエルシー Boron-containing nucleus agent for polyarylene sulfide

Also Published As

Publication number Publication date
JP3644713B2 (en) 2005-05-11

Similar Documents

Publication Publication Date Title
JP6483508B2 (en) Hexagonal boron nitride powder and method for producing the same
JP2012504103A (en) Production of solar grade silicon from silicon dioxide
JPH08217424A (en) Hexagonal boron nitride powder and its production
KR102574046B1 (en) Low-temperature production method of boron carbide
JP3669818B2 (en) Hexagonal boron nitride powder
JPS6111886B2 (en)
KR101549477B1 (en) Manufacturing Method of High Purity SiC Powder
JP5043632B2 (en) Method for producing hexagonal boron nitride
JP2023049689A (en) Method for producing modified hexagonal boron nitride powder and modified hexagonal boron nitride powder
JP3647079B2 (en) Method for producing hexagonal boron nitride powder
JPH0510282B2 (en)
JPH10203806A (en) Production of boron nitride powder
JPH0524849B2 (en)
JPH01103960A (en) Production of boron nitride sintered compact
JPH10316469A (en) Powdery magnesium silicide nitride and its production
JPS62100403A (en) Production of fine powder of hexagonal boron nitride having high purity
JPS61168567A (en) Manufacture of silicon carbide sintered body
JPS602244B2 (en) Manufacturing method of rhombohedral boron nitride
JP2023049688A (en) Method for producing modified hexagonal boron nitride powder and modified hexagonal boron nitride powder
JP4025810B2 (en) Method for producing silicon nitride particles
JPH1129308A (en) Hexagonal boron nitride powder and its use
JP2024037327A (en) Method for producing hexagonal boron nitride
JP2022080053A (en) Silicon nitride powder and its production method, and method for producing sintered silicon nitride body
JPH058123B2 (en)
JPS6158806A (en) Manufacture of high-purity hexagonal boron nitride powder

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040831

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20041122

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050105

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20050201

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20050201

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090210

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090210

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100210

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110210

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120210

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120210

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130210

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140210

Year of fee payment: 9

EXPY Cancellation because of completion of term