JPS62100404A - Production of pulverous hexagonal boron nitride having high purity - Google Patents

Production of pulverous hexagonal boron nitride having high purity

Info

Publication number
JPS62100404A
JPS62100404A JP23950385A JP23950385A JPS62100404A JP S62100404 A JPS62100404 A JP S62100404A JP 23950385 A JP23950385 A JP 23950385A JP 23950385 A JP23950385 A JP 23950385A JP S62100404 A JPS62100404 A JP S62100404A
Authority
JP
Japan
Prior art keywords
particle size
boron nitride
hexagonal boron
high purity
heating
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
JP23950385A
Other languages
Japanese (ja)
Other versions
JPH0535084B2 (en
Inventor
Takahisa Koshida
孝久 越田
Takeshi Ogasawara
小笠原 武司
Kimiaki Sasaki
王明 佐々木
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.)
JFE Steel Corp
JFE Refractories Corp
Original Assignee
Kawasaki Refractories Co Ltd
Kawasaki Steel Corp
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 Kawasaki Refractories Co Ltd, Kawasaki Steel Corp filed Critical Kawasaki Refractories Co Ltd
Priority to JP23950385A priority Critical patent/JPS62100404A/en
Publication of JPS62100404A publication Critical patent/JPS62100404A/en
Publication of JPH0535084B2 publication Critical patent/JPH0535084B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To produce fine powder of hexagonal boron nitride having high purity and optional particle size by heating fine powder of crude hexagonal boron nitride at an appropriate temp. and under appropriate pressure in nonoxidizing atmosphere, then heating at an appropriate temp. under reduced pressure. CONSTITUTION:Fine powder of crude hexagonal boron nitride synthesized at ca. 800-1,200 deg.C is heated at 1,200-1,800 deg.C under >=20Torr in nonoxidizing atmosphere. By this treatment, the particle size is grown to some degree obtaining boron nitride having 100Angstrom -5mum primary particle size depending on the temp., and impurities such as B-O-N, etc., are transformed to BN and B2O3. Then, BN, etc., are removed by heating at 1,600-2,000 deg.C under <=20Torr in nonoxidizing atmosphere. By this method, fine powder of hexagonal boron nitride having high purity and primary particle size controlled to desired particle size is obtd. by removing impurities such as B2O3, etc., by evaporation without causing the growth of particle size.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は六方晶窒化硼素(以’l’−h−BNと記載す
る)の製造法に関するものであり、−次粒子径と純度を
制御できる技術をダ、えるものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for producing hexagonal boron nitride (hereinafter referred to as 'l'-h-BN), which involves controlling the -order particle size and purity. It's about getting the technology you can.

〔従来の技術〕[Conventional technology]

h−BNは白色で黒鉛と類似した六方晶の層状構造をな
し、多種の特徴を有している。特に熱伝導性、電気絶縁
性、耐食性、潤滑性、耐熱性、機械加工性などについて
は優れており、これらの性質を生かして用途は多岐に1
1っている。粉末としての用途にはプラスチック添加剤
、潤滑剤などがあり、成形体および複合材としては治J
し電気絶縁材、型材などの用途がある。
h-BN is white and has a hexagonal layered structure similar to graphite, and has various characteristics. In particular, it has excellent thermal conductivity, electrical insulation, corrosion resistance, lubricity, heat resistance, and machinability, and these properties can be used for a wide variety of applications.
1 is there. Applications as a powder include plastic additives and lubricants, and as molded bodies and composite materials, it can be used as a therapeutic agent.
It is used as electrical insulation material, mold material, etc.

このように用途の広いh−BNを合成する方法は種々考
案されているが、現在T業的に採用されている方法は、 (1)硼砂と尿素の混合物をアンモニア雰囲気中で80
0℃以り、に加熱する方法(特公昭38−161O)、 (2)硼酸または酸化硼素と燐酸カルシウムを混合し、
アンモニアで窒化する方法、 (3)硼酸と含窒素化合物(尿素、メラミン、塩化アン
モニウム、ジシアンジアミド等)を1600℃以しに加
熱する方法(特許IQ448−14559)、 (4)三塩化硼素とアンモニアにより気相合成する方法
Various methods have been devised to synthesize h-BN, which has a wide range of uses, but the method currently used in the T industry is: (1) A mixture of borax and urea is synthesized in an ammonia atmosphere at 80%
A method of heating to below 0℃ (Japanese Patent Publication No. 38-161O), (2) Mixing boric acid or boron oxide and calcium phosphate,
(3) A method of heating boric acid and a nitrogen-containing compound (urea, melamine, ammonium chloride, dicyandiamide, etc.) to 1600°C or higher (Patent IQ448-14559), (4) A method of nitriding with ammonia, Method of vapor phase synthesis.

などが主なものである。etc. are the main ones.

(5)さらに純度90@星%程度のh−BN番、″−フ
ルカリ金属化合物を添加して1ooo℃以l−に加熱す
ることにより99屯品%以l−にまで高純度化する方法
(特公昭47−26600)がある。
(5) Furthermore, h-BN number with a purity of about 90@star%,''- a method of adding a fulkaline metal compound and heating it to 100°C or less to improve the purity to 99 tons% or less ( Special Publication No. 47-26600).

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

」−記(1)の方法は、900℃程度で粗製BNを製造
しアルカリ分を水洗除去した後、非酸化性雰囲気中で1
600℃〜2000℃に再加熱して不純物を蒸発除去す
ることで高純化する。高純化の工程h−BN粒子は結晶
の成長を生じ一次粒子径は1〜5pLmになる。
”-Method (1) is to produce crude BN at about 900°C, remove alkaline content by washing with water, and then heat it in a non-oxidizing atmosphere for 1 hour.
It is highly purified by reheating to 600°C to 2000°C to evaporate and remove impurities. High purification process h-BN particles undergo crystal growth and have a primary particle size of 1 to 5 pLm.

」二記(2)、(3)の方法においても同様に高純化過
程で粒成長を生ずるために任意に粒aを制御できない欠
点があった。
Similarly, the methods described in Section 2 (2) and (3) also have the drawback that grain growth occurs during the high purification process, making it impossible to arbitrarily control grain a.

次に、(4)の方法は(1)〜(3)の方法と異なり、
気相合成方法のため高純度で微細な粒径のり、−BNを
得ることができるが、N料の五塩化硼素が高価であるた
め、製造コストが高くつく欠点があった。
Next, method (4) is different from methods (1) to (3),
Because of the gas phase synthesis method, it is possible to obtain -BN with high purity and a fine particle size, but since boron pentachloride as the N material is expensive, there is a drawback that the manufacturing cost is high.

また(5)の粗製BNにアルカリ金属化合物な添加して
高純化する方法では、(1)〜(3)の製造方法で得ら
れるh−BNよりも微細な結晶粒のものも得ることがで
きるが、添加【7たアルカリ金属が合成炉に付着して製
造り一好ましくないなどの欠点があった。
In addition, in the method (5) of adding an alkali metal compound to the crude BN for high purification, it is possible to obtain h-BN with finer grains than the h-BN obtained by the production methods (1) to (3). However, there were drawbacks such as the fact that the added alkali metal adhered to the synthesis furnace, making it undesirable during production.

本発明は、h−BNの高純化処理■゛程においてその−
・次粒子−径の大きさを所ψのイめにコントロールする
ことをIIT能とするh−BNの製造方法を提供するこ
とを目的とする。
The present invention is directed to the -
- It is an object of the present invention to provide a method for producing h-BN in which the IIT function is to control the size of the secondary particle diameter to a certain degree ψ.

〔問題点を解決する手段〕[Means to solve problems]

本発明者らは、従来技術を補うべく鋭i r:夫を屯ね
た結果、95重量%以[−の純度で・成粒−f径をコン
トロールできる技術を開発するに〒つだ。
As a result of extensive research to supplement the conventional technology, the inventors of the present invention have developed a technology that can control the granulation diameter with a purity of 95% by weight or more.

この技術開発の動機となったのはh−BNの高純化を2
0To r r以下の減圧Fで行えば粒成長を生ずるこ
となく高純化を行うことができることを発見した点にあ
る。つまりh−BNの粒成長の[程と高純化「程を独立
して行えば、種々の一次粒子径を有する高純度h−BN
を容易に製造することができる。h−BNは熱処理温度
と共に成長して行くので、所望の一次粒子径に成長さゼ
だ後、雰囲気を20Torr以下に保って加熱処理を進
めることによって、結晶粒の成長を抑えながら高純化を
行うことができ、高純度で所91の・次粒子径のh−B
NをftJることができる。
The motivation for developing this technology was to improve the purity of h-BN.
The main point lies in the discovery that high purity can be achieved without causing grain growth if the process is carried out at a reduced pressure F of 0 Torr or less. In other words, if the grain growth and purification processes of h-BN are performed independently, high-purity h-BN with various primary particle diameters can be obtained.
can be easily manufactured. Since h-BN grows with the heat treatment temperature, after it has grown to the desired primary particle size, by proceeding with the heat treatment while keeping the atmosphere below 20 Torr, high purity can be achieved while suppressing the growth of crystal grains. High purity h-B with a particle size of 91.
N can be ftJ.

本発明による・次粒子径を制御しながらh−BNを高純
化する方〃、についてさらに其体的に述べる。原料であ
る粗製h−BNは通常800℃〜1200℃で合成して
得られたものであり、結晶は完全には六方晶となってお
らず乱層構造を有している。結晶f−の大きさLc(7
振炭素材料117委Ll会資料による方法で測定した値
)は50人〜100人と小さく、−次粒子径の大きSも
100人前後の微粒になっている。純度については試料
中の窒素分析から求めると50〜95重縫%の範囲であ
った。不純物としては#素が殆どであり、存在形態とし
ては硼酸アンモニウム、酸化硼素などがX線回折により
同定された。
The method of highly purifying h-BN while controlling the secondary particle diameter according to the present invention will be described in more detail. Crude h-BN, which is a raw material, is usually synthesized at 800°C to 1200°C, and its crystals are not completely hexagonal but have a turbostratic structure. The size of crystal f- Lc (7
The value measured by the method according to the materials of the Carbon Materials 117 Committee Ll Association) is small, ranging from 50 to 100 particles, and the -order particle size S is also fine, around 100 particles. The purity was determined from nitrogen analysis in the sample and was in the range of 50 to 95%. Most of the impurities were # elements, and the existing forms of ammonium borate, boron oxide, etc. were identified by X-ray diffraction.

これらの不純物を除去する方法としては、加熱処理によ
り蒸気として蒸発除去する方法が採られる。しかし加熱
処理中に不純物が液相を生成し、h−BNの高純化とと
もに結晶子も成長し、−次粒子径も大きくなっていった
。例えば硼砂と尿素から900℃で合成した粗製h−B
N (純1190屯星%、 L e = 150人)を
水洗し、アルカリ分を除去した後、加熱するとL cは
1800℃で約1000人に成長した。これ以F、の温
度では結晶子の成長は見られなかった。硼酸とジシアン
ジアミドなどから合成した粗製h−B Nを使用17て
も同様な傾向であった。このときのh−BNNi度は9
9.21TjM−%で−・次粒子径は3μ、mあった。
As a method for removing these impurities, a method of evaporating them as steam through heat treatment is adopted. However, impurities generated a liquid phase during the heat treatment, and as h-BN became highly purified, crystallites also grew, and the secondary particle size also increased. For example, crude h-B synthesized from borax and urea at 900℃
When N (1190 tonxing% pure, L e = 150 people) was washed with water to remove alkaline content and heated, L c grew to about 1000 people at 1800°C. No growth of crystallites was observed at temperatures below F. A similar tendency was observed when crude h-BN synthesized from boric acid, dicyandiamide, etc. was used. At this time, h-BNNi degree is 9
At 9.21 TjM-%, the particle size was 3 μm.

このように高純度のh−BNを得ようとすると一次粒子
も成長するため、実験名の札望する一次粒子径で高純度
なh−BNを得ることはできなかった。
In this way, when trying to obtain h-BN with high purity, the primary particles also grow, so it was not possible to obtain h-BN with high purity with the primary particle diameter desired by the name of the experiment.

この点を解決すべく検討17た結果、粒成長の原因であ
る液相を彫成する不純物を急速に除去する方法が必要で
あった。除去力U:とじては減圧下で熱処理すれば不純
物の蒸発速度が大きくなり粒成長を生じない。減圧の程
度は圧力が20Torr以ドであれば、粒成長はほとん
ど生じていないことが明らかとなった。
As a result of studies17 to solve this problem, it was found that there was a need for a method to rapidly remove impurities that carve the liquid phase, which is the cause of grain growth. Removal power U: If heat treatment is performed under reduced pressure, the evaporation rate of impurities will be high and grain growth will not occur. It has become clear that grain growth hardly occurs when the pressure is reduced to 20 Torr or higher.

しかし900℃〜l 200 ’Oで合成した和製h−
BNを20Torr以ドのu圧ドで1200℃〜180
0℃の加熱処理しても純度は95重都%以■−にはなら
なかった。原因としては粗製h−BN中には多l、lの
耐素がB−0−Nなどの中間体の形でり、−B N中に
含イ1されているため減圧下の加熱処理では除去できな
かったと考えられる。
However, the Japanese h-
BN at 1200℃ to 180℃ at a pressure of 20Torr or more
Even after heat treatment at 0°C, the purity did not reach 95% or higher. The reason for this is that crude h-BN contains a large amount of resistant element in the form of intermediates such as B-0-N, and is contained in -BN, so it cannot be heated during heat treatment under reduced pressure. It seems likely that it could not be removed.

常圧下である程度粒J&長を生じさせ、ll−0−Nな
どの中間体をBNとB2O3に転化させて、蒸発除去す
ることが必要になる。20Torr以上の圧力(通常は
常圧)−ドで1200℃〜1800℃に加熱することに
より、温度に対応してlOOλ〜5ルmの範囲の−・次
粒子=径を有するBNとし、しかるのち20Torr以
ドの減圧ドで1600℃〜2000℃に加熱することに
よってBN中のB20ヨなどの不純物を蒸発除去する。
It is necessary to generate grain J&length to some extent under normal pressure, convert intermediates such as 11-0-N into BN and B2O3, and remove them by evaporation. By heating to 1200°C to 1800°C at a pressure of 20 Torr or more (usually normal pressure), BN is made into BN having a particle diameter in the range of lOOλ to 5 m depending on the temperature, and then Impurities such as B20 in BN are evaporated and removed by heating to 1600° C. to 2000° C. under reduced pressure of 20 Torr or higher.

このようにして高純化を図れば、種々の−・次$1″L
r−径を有した高純度h−BNを得ることができる。
If high purity is achieved in this way, various −・Next $1″L
High purity h-BN with r-diameter can be obtained.

粒成長の工程で20Torr以上としたのは20Tor
r以トが粒成長が起こる範囲であり、1200℃から粒
成長が始まり、1800℃を超えると粒成長が1トまる
The temperature of 20 Torr or higher in the grain growth process is 20 Torr.
The range below r is the range in which grain growth occurs, and grain growth begins at 1200°C, and when the temperature exceeds 1800°C, grain growth decreases by 1.

次いで不純物除去1程における減圧条件は、N2等の非
酸化性雰囲気が20Torr以−ドとする。しかし、加
熱中に不純物の8203゜NI(3,Goなどが出てく
る際に充填層内部では20Torrよりも高くなる場合
もあるが、非酸化性雰囲気が20Torr以ドであれば
、不純物の系外への除去速1■も大きく、粒J&長は抑
制される。
Next, the reduced pressure conditions in the first stage of impurity removal are such that the non-oxidizing atmosphere such as N2 is 20 Torr or higher. However, when impurities such as 8203°NI (3, Go, etc.) come out during heating, the temperature may become higher than 20 Torr inside the packed layer, but if the non-oxidizing atmosphere is 20 Torr or higher, the impurity The removal speed 1■ to the outside is also large, and the grain J&length is suppressed.

20Torr以下の減圧下での加熱温度は、粒成長工程
温度より高いのが好ましい。この範囲は、不純物が完全
に除去できる1600℃以(−が好ましく、ト限は容器
として用いる黒鉛とBNが反応I7てB4Cを生ずる温
度以下とする必要があり、2000℃以fである。
The heating temperature under reduced pressure of 20 Torr or less is preferably higher than the grain growth process temperature. This range is preferably 1,600° C. or below (- is preferable) at which impurities can be completely removed, and the limit must be below the temperature at which the graphite used as the container and BN react to form B4C, and is 2,000° C. or below.

〔実施例〕〔Example〕

実施例1〜4 無水硼砂1.0kgと尿素2.0 k gを混合しアン
モニア雰囲気中で900’OX2時間処理した後水洗し
てナトリウム分を除去した生成物(BN純度91.3市
U%、−次粒子径130人)を黒鉛るつぼに充填し、N
2雰囲気中で常圧下でそれぞれ1200℃、1400℃
、l 600 ’011800℃に1時間保持した後、
0.1Torrの減圧下に雰囲気を保った後、1aoo
’cで2時間加熱処理を行った。その結果を第1表に示
す。第1表から明らかなように、95屯に%以1−の高
純INで種々な結晶粒を有した11−B Nを製造する
ことができた。
Examples 1 to 4 1.0 kg of anhydrous borax and 2.0 kg of urea were mixed and treated in an ammonia atmosphere at 900'OX for 2 hours, followed by washing with water to remove the sodium content (BN purity 91.3 city U%). , -order particle size 130 people) was filled into a graphite crucible, and N
1200℃ and 1400℃ under normal pressure in two atmospheres, respectively.
, l 600 '011 After holding at 1800°C for 1 hour,
After maintaining the atmosphere under a reduced pressure of 0.1 Torr, 1aoo
Heat treatment was performed for 2 hours at 'c. The results are shown in Table 1. As is clear from Table 1, it was possible to produce 11-BN having various crystal grains with high purity IN of less than 1% in 95 tons.

比較例−1 実施例−1と同一の方法により製造した粗製h−BNを
0.ITOrrの減圧下で1soo’c、2時ff!1
8処理を行ったところ純度は93重U%で−・次粒子径
は160人であった。
Comparative Example-1 Crude h-BN produced by the same method as Example-1 was mixed with 0. 1 soo'c, 2 o'clock ff under reduced pressure of ITOrr! 1
After 8 treatments, the purity was 93% by weight and the particle size was 160.

比較例−2 実施例−1と同一の方法により製造した粗製h  B 
N lid N 2雰囲気大気圧ドで1100℃でlh
r加熱処理した後、0.ITorr(7)M圧下C18
00”0XZhr熱処理を行ったところ純度は94.2
市v%で・次粒子径は210人であった。
Comparative Example-2 Crude hB produced by the same method as Example-1
N lid N2 atmosphere atmospheric pressure at 1100℃ lh
r After heat treatment, 0. ITorr (7) M pressure C18
00" Purity was 94.2 after 0XZhr heat treatment.
The particle size was 210 people in city v%.

〔発明の効果〕〔Effect of the invention〕

本発明力?J:により、高純度化したh−BNの粒径を
所望の値にコントロールすることができ、各種の用途に
広く対応できるh−BNの製造が可能となった。
Inventiveness? J: allows the particle size of highly purified h-BN to be controlled to a desired value, making it possible to produce h-BN that can be widely used in various applications.

Claims (1)

【特許請求の範囲】 1 20Torr以上の非酸化性雰囲気中で、粗製六方
晶窒化硼素微粉末を1200℃〜 1800℃の温度で加熱し、しかる後、これを20To
rr以下の非酸化性雰囲気中において1600℃〜20
00℃に加熱することを特徴とする高純度六方晶窒化硼
素粉末の製造方法。
[Claims] 1. In a non-oxidizing atmosphere of 20 Torr or more, crude hexagonal boron nitride fine powder is heated at a temperature of 1200°C to 1800°C, and then heated to 20Torr.
1600°C to 20°C in a non-oxidizing atmosphere below rr
A method for producing high-purity hexagonal boron nitride powder, the method comprising heating to 00°C.
JP23950385A 1985-10-28 1985-10-28 Production of pulverous hexagonal boron nitride having high purity Granted JPS62100404A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23950385A JPS62100404A (en) 1985-10-28 1985-10-28 Production of pulverous hexagonal boron nitride having high purity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23950385A JPS62100404A (en) 1985-10-28 1985-10-28 Production of pulverous hexagonal boron nitride having high purity

Publications (2)

Publication Number Publication Date
JPS62100404A true JPS62100404A (en) 1987-05-09
JPH0535084B2 JPH0535084B2 (en) 1993-05-25

Family

ID=17045754

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23950385A Granted JPS62100404A (en) 1985-10-28 1985-10-28 Production of pulverous hexagonal boron nitride having high purity

Country Status (1)

Country Link
JP (1) JPS62100404A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0578106A (en) * 1989-12-08 1993-03-30 Rhone Poulenc Chim Monodisperse hexagonal boron nitride showing very high purity level in respect of metal and oxygen and its preparation
JPH05186205A (en) * 1992-01-08 1993-07-27 Kawasaki Steel Corp Hexagonal boron nitride powder and its production
JPH08225310A (en) * 1995-02-23 1996-09-03 Denki Kagaku Kogyo Kk Production of boron nitride powder of hexagonal system
JP2009177011A (en) * 2008-01-25 2009-08-06 Ferrotec Ceramics Corp Conductive member, and component and equipment using it
WO2011043082A1 (en) * 2009-10-09 2011-04-14 水島合金鉄株式会社 Hexagonal boron nitride powder and method for producing same
JP2014094878A (en) * 2012-10-11 2014-05-22 Mizushima Ferroalloy Co Ltd High oil absorptive boron nitride powder excellent in heat release and cosmetics
US20150209248A1 (en) * 2012-09-28 2015-07-30 Mizushima Ferroalloy Co., Ltd. Hydrophilic and highly oil absorbent boron nitride powder, method for manufacturing the same, and cosmetic

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0578106A (en) * 1989-12-08 1993-03-30 Rhone Poulenc Chim Monodisperse hexagonal boron nitride showing very high purity level in respect of metal and oxygen and its preparation
JPH05186205A (en) * 1992-01-08 1993-07-27 Kawasaki Steel Corp Hexagonal boron nitride powder and its production
JPH08225310A (en) * 1995-02-23 1996-09-03 Denki Kagaku Kogyo Kk Production of boron nitride powder of hexagonal system
JP2009177011A (en) * 2008-01-25 2009-08-06 Ferrotec Ceramics Corp Conductive member, and component and equipment using it
WO2011043082A1 (en) * 2009-10-09 2011-04-14 水島合金鉄株式会社 Hexagonal boron nitride powder and method for producing same
JP2011098882A (en) * 2009-10-09 2011-05-19 Mizushima Ferroalloy Co Ltd Hexagonal boron nitride powder and method for producing the same
CN102574684A (en) * 2009-10-09 2012-07-11 水岛合金铁株式会社 Hexagonal boron nitride powder and method for producing same
US8679429B2 (en) 2009-10-09 2014-03-25 Mizushima Ferroalloy Co., Ltd. Hexagonal boron nitride powder having specific bulk density and residual Fe particles, and method for producing same
US20150209248A1 (en) * 2012-09-28 2015-07-30 Mizushima Ferroalloy Co., Ltd. Hydrophilic and highly oil absorbent boron nitride powder, method for manufacturing the same, and cosmetic
US9433565B2 (en) * 2012-09-28 2016-09-06 Mizushima Ferroalloy Co., Ltd. Hydrophilic and highly oil absorbent boron nitride powder, method for manufacturing the same, and cosmetic
JP2014094878A (en) * 2012-10-11 2014-05-22 Mizushima Ferroalloy Co Ltd High oil absorptive boron nitride powder excellent in heat release and cosmetics

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