JPS5815012A - Manufacture of cubic system boron nitride - Google Patents

Manufacture of cubic system boron nitride

Info

Publication number
JPS5815012A
JPS5815012A JP11358981A JP11358981A JPS5815012A JP S5815012 A JPS5815012 A JP S5815012A JP 11358981 A JP11358981 A JP 11358981A JP 11358981 A JP11358981 A JP 11358981A JP S5815012 A JPS5815012 A JP S5815012A
Authority
JP
Japan
Prior art keywords
catalyst
boron nitride
cbn
yield
cubic system
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
JP11358981A
Other languages
Japanese (ja)
Other versions
JPS6366254B2 (en
Inventor
Hiroshi Ishizuka
博 石塚
Nobutaka Nakaaki
仲秋 伸孝
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.)
Ishizuka Research Institute Ltd
Original Assignee
Ishizuka Research Institute 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 Ishizuka Research Institute Ltd filed Critical Ishizuka Research Institute Ltd
Priority to JP11358981A priority Critical patent/JPS5815012A/en
Publication of JPS5815012A publication Critical patent/JPS5815012A/en
Publication of JPS6366254B2 publication Critical patent/JPS6366254B2/ja
Granted legal-status Critical Current

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  • Catalysts (AREA)

Abstract

PURPOSE:To obtain cubic system BN having a large particle size and well developed crystal faces in a high yield by using a catalyst prepared by adding CaH2 to Li3BN2 when hexagonal system BN is converted into cubic system BN by holding it in the thermodynamically stable region. CONSTITUTION:CaH2 is added to Li3BN2 to prepare a catalyst, and the catalyst is mixed with hexagonal system BN. The pressure of the mixture is raised from about 47kb to about 51kb in about 13min while keeping the temp. at about 1,500 deg.C, and the temp. and pressure are dropped. The resulting cubic system BN is brown and has high transparency. The particle size is large, most of the particles have >=50mum size, and even particles having >=150mum size are contained. The yield is as high as about 40%. The preferred percentage of CaH2 added to Li3BN2 is about 1.5-35wt%.

Description

【発明の詳細な説明】 本発明は触媒を用いて六方晶窒化硼素を立方晶窒化硼素
に変換する方法に関する。ものであり、特に結晶性の良
い大粒の立方晶窒化硼素を高収率で得る方法に関するも
のでおる。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for converting hexagonal boron nitride to cubic boron nitride using a catalyst. The present invention relates to a method for obtaining large grain cubic boron nitride with particularly good crystallinity at a high yield.

立方晶窒化硼素(以下cBNと略称する)はダイヤモン
ドに次ぐ硬度を持つ上に、熱的、化学的性質はダイヤモ
ンドよりも秀れているため、近年、特に焼き入れ鋼の研
削、研麿用砥粒として需要が伸びている物質である。
Cubic boron nitride (hereinafter abbreviated as cBN) has a hardness second only to diamond, and has better thermal and chemical properties than diamond. It is a substance whose demand is increasing in the form of grains.

cBNを製造する方法としては種々のものが発表されて
いるが、従来からよく知られている方法は、六方晶窒化
硼素(以下hBNと略称する)を触媒の存在下でcBN
の熱力学的安定領域内に保持することによってcBNに
変換するに際し、触媒としてアルカリ金属、アルカリ土
類金属、これらを含む合金、これらの窒化物、硼化物等
を用いる方法である。
Various methods have been announced for producing cBN, but a well-known method is to produce cBN from hexagonal boron nitride (hereinafter abbreviated as hBN) in the presence of a catalyst.
This method uses alkali metals, alkaline earth metals, alloys containing them, nitrides, borides, etc. of these metals as catalysts when converting to cBN by maintaining the cBN within the thermodynamic stability region of cBN.

触媒物質としては窒化物、硼化物がよく調べられており
、特KLi、NあるいはLi1BNlが有効であるとさ
れている。しかし、これらの触媒を使って得られる従来
のcBN結晶は一般に50μ以下の微粒子で結晶性も良
くなく、研削砥粒として、その性能を十分発揮するまで
には至っていなかった。し九がって、結晶面のよく発達
した大粒のcBNを製造する技術が望まれていた。
As catalyst materials, nitrides and borides have been well investigated, and KLi, N or Li1BN1 are said to be particularly effective. However, conventional cBN crystals obtained using these catalysts generally have fine particles of 50 μm or less and do not have good crystallinity, and have not been able to fully demonstrate their performance as grinding abrasive grains. Therefore, a technology for producing large grains of cBN with well-developed crystal planes has been desired.

本発明は、前記のような触媒を改良することによって結
晶面のよく発達した大粒のcBNを高収率で製造する方
法を提供するものである。
The present invention provides a method for producing large-grained cBN with well-developed crystal planes at a high yield by improving the above-mentioned catalyst.

即ち、本発明の方法は、Li5BN*に、CaH。That is, in the method of the present invention, CaH is added to Li5BN*.

を添加したものを触媒として用い、これをhBNと併存
せしめて、cBNの熱力学的安定領域内の温度・圧力に
保持することによって、cBNを得ることを特徴とする
It is characterized in that cBN is obtained by using as a catalyst a catalyst containing hBN, coexisting with hBN, and maintaining the temperature and pressure within the thermodynamic stability range of cBN.

発明者らの実験によれば、LtsBN*だけをhBNと
混合して、温度を約1,500℃に保ちながら圧力を約
47 kbから51 kbまで13分間かけてゆっくり
上げた後に、温度を下げ、圧力を下げることによって得
られたcBNは不透明な黄土色であり、粒径は50μ以
下の小さいものばかりであった。さらに収率も約181
と低いものであった。−力木発明方法に従ってLi、B
N−にCa H重を3.75wtts添加したものを触
媒として用い、他の条件は全く同様に操作した場合、得
られたCBNは、褐色で透明度が高く、特に粒径が大き
くなってほとんどの粒子が50μ以上であり、中には1
50μを越える粒子もあった。収率も約40チと高くな
った。
According to the inventors' experiments, only LtsBN* was mixed with hBN, and the pressure was slowly raised from about 47 kb to 51 kb over 13 minutes while maintaining the temperature at about 1,500 °C, and then the temperature was lowered. The cBN obtained by lowering the pressure was an opaque ocher color, and the particle size was mostly small, less than 50 μm. Furthermore, the yield is about 181
It was low. - Li, B according to the strength wood invention method
When 3.75 wtts of Ca H weight was added to N- as a catalyst and the other conditions were the same, the obtained CBN was brown in color and highly transparent. The particles are 50μ or more, and some of them are 1
Some particles exceeded 50μ. The yield was also as high as about 40 cm.

触媒としてLi、BN=にCa Htを添加したものを
用いることの利点は、先ず第1にcBNの粒径が大きく
なり易く収率も高くなることである。他に結晶中のクラ
ックが少なくなり、透明度が良くなり又、結晶面が発達
し易いなど、研削砥粒に適した結晶になるという利点も
ある。
The advantage of using Li, BN= with CaHt added as a catalyst is that the particle size of cBN tends to increase and the yield increases. Other advantages include fewer cracks in the crystal, improved transparency, and easier development of crystal faces, making the crystal suitable for grinding abrasive grains.

実験によれば、L is B Ntに添加するCaH,
の割合は重量比で1.5〜35チが好ましい。CaH。
According to experiments, CaH added to Li is B Nt,
The ratio by weight is preferably 1.5 to 35 inches. CaH.

の量が1.5−未満セはCa出を添加することの利点が
現れず、L i = B N掌だけの時と同様、粒径も
小さく、収率も低い。Ca H*の割合が1.5〜35
チの範囲ではcBNの収率は、20〜50%の幅で、雌
ぼ一定の水準が得られ、時には60チ近い高収率になる
こともある。CaH,が多くなるに従って結晶の色は黄
褐色から茶褐色へと変化するが多過ぎると、透明度が悪
くなることもあり、粒径もやや小さくなる。CaH*の
割合が35%よりも多くなると、無添加の時と同じ程度
に結晶の粒径が小さくなり、収率も低くなる。
If the amount is less than 1.5, the advantage of adding Ca does not appear, and the particle size is small and the yield is low, as in the case of only Li = BN. The ratio of CaH* is 1.5 to 35
In the range of 60%, the yield of cBN ranges from 20% to 50%, and a constant level of cBN can be obtained, and sometimes the yield can be as high as 60%. As the amount of CaH increases, the color of the crystal changes from yellowish brown to brownish brown, but if it is too much, the transparency may deteriorate and the particle size becomes slightly smaller. When the proportion of CaH* exceeds 35%, the grain size of the crystals becomes small to the same extent as when no additive is added, and the yield also becomes low.

次に実施例について説明する。Next, an example will be described.

実施例 L t s B Ng 200 ”I、Ca 
Ha 7.5 ”?およびhHN60011をよく混合
して反応容器に充填し高温高圧をかけた。先ず圧力を4
7kbまで上げた時点で温度を約1.500℃に保ち、
47kbで5分、48kb、49kb、50kbおよび
51 kbで各々2分間保持するというように圧力をゆ
っくり上げた。温度を下げ、圧力を下げて反応物を回収
すると、褐色で透明な結晶のよく発達したcBNが24
0■得られた。収率は40チである。y倚られたcBN
をTyler呼称で270メソシユ、140メツシユ、
100メソシーのふるいを用いて粒度を測定した結果を
次表に示す。比較のためCa Htを添加しない場合の
結果を併記した。
Example L t s B Ng 200 “I, Ca
Ha 7.5"? and hHN60011 were mixed well and filled into a reaction vessel, and high temperature and pressure were applied. First, the pressure was increased to 4.
When the temperature reaches 7kb, keep the temperature at about 1.500℃,
The pressure was slowly increased by holding 47 kb for 5 minutes, 48 kb, 49 kb, 50 kb and 51 kb for 2 minutes each. When the temperature and pressure are lowered and the reactants are collected, brown, transparent, crystalline, well-developed cBN is obtained at 24
0■ obtained. Yield is 40 g. y chewed cBN
270 meshes, 140 meshes, under the name of Tyler.
The particle size was measured using a 100 Mesosie sieve and the results are shown in the table below. For comparison, the results when CaHt was not added are also shown.

ここで圧力測定は検圧素子としての金属の電気抵抗値の
変化によるものであl)、Bat−厘転移を55kb、
Tロー厘転移を36.7kbとし次ものである。
Here, the pressure measurement is based on the change in the electrical resistance value of the metal used as the pressure detection element.
The T-row metastasis is 36.7 kb and is as follows.

温度は反応容器内にPt−Pt 13%Rhの熱電対を
挿入して熱電対指示温度と電圧との関係を前もって求め
ておき、実際の合成にあたっては電力値から温度を推足
した。
The temperature was determined in advance by inserting a Pt-Pt 13%Rh thermocouple into the reaction vessel and determining the relationship between the temperature indicated by the thermocouple and the voltage, and in the actual synthesis, the temperature was estimated from the electric power value.

CaH,の代りにCa N tをL l * B Ng
に添加して触媒とした場合には結果はLi、BN、のみ
を用いた時と変わらなかった。
CaNt instead of CaH, L l * B Ng
When Li and BN were added to form a catalyst, the results were the same as when Li and BN were used alone.

Ca H禦のみを触媒に用いた場合にも得られるCBN
の収率は低く結晶粒径も小さいので、本件発明の効果は
、L i = B NgとCaH,を組み合わせた点に
よるものと思われる。
CBN obtained even when using only CaH as a catalyst
Since the yield of is low and the crystal grain size is small, it is thought that the effect of the present invention is due to the combination of L i = B Ng and CaH.

実施例の温度圧力と同じ条件で、触媒として、Ca5B
*NiとCa Haとの混合物およびLtsBI’Lと
LiHとの混合物を用いて比較実験をしたところ、どち
らの場合もcBNt:を得られなかった。又Ca5lL
N*のみを触媒として用いて同様の実験をしたところ、
得られたcBNli粒径が全ぺて30声以下と小さく収
率4123チと低かつ比。
Under the same temperature and pressure conditions as in the example, Ca5B was used as a catalyst.
*When a comparative experiment was conducted using a mixture of Ni and CaHa and a mixture of LtsBI'L and LiH, cBNt: could not be obtained in either case. Also Ca5lL
When we conducted a similar experiment using only N* as a catalyst, we found that
The cBNli particle size obtained was small, less than 30 tones in total, and the yield was low at 4123 tones.

C’as Bt N4の使用は特公昭55−60008
で公知であり、その実施例によれば、56000気圧、
1500℃の条件、又U60000気圧、1750℃の
条件などにおいては、有効な触媒機能−を示すとさ−れ
ている。従って本発明による触媒はこれら比°較実験を
行なった触媒よりも低圧力下でも効果的に機能すること
が明らかである。
The use of C'as Bt N4 was approved by Special Publication No. 55-60008.
According to its examples, 56,000 atmospheres,
It is said that it exhibits an effective catalytic function under conditions of 1,500°C, U60,000 atmospheric pressure, and 1,750°C. It is therefore clear that the catalyst according to the invention functions more effectively at lower pressures than the catalysts used in these comparative experiments.

Claims (1)

【特許請求の範囲】[Claims] 水素化カルシウム金添加した窒化硼素リチウムを触媒と
して用い、この触媒を六方晶窒化硼素と併存せしめて、
立方晶窒化硼素の熱力学的安定領域内に保持することに
よって立方晶窒化硼素を得ることを特徴とする立方晶窒
化硼素の製造法。
Using lithium boron nitride to which calcium hydride gold is added as a catalyst, this catalyst is made to coexist with hexagonal boron nitride,
A method for producing cubic boron nitride, characterized in that cubic boron nitride is obtained by maintaining the cubic boron nitride within a thermodynamically stable region.
JP11358981A 1981-07-22 1981-07-22 Manufacture of cubic system boron nitride Granted JPS5815012A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11358981A JPS5815012A (en) 1981-07-22 1981-07-22 Manufacture of cubic system boron nitride

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11358981A JPS5815012A (en) 1981-07-22 1981-07-22 Manufacture of cubic system boron nitride

Publications (2)

Publication Number Publication Date
JPS5815012A true JPS5815012A (en) 1983-01-28
JPS6366254B2 JPS6366254B2 (en) 1988-12-20

Family

ID=14616041

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11358981A Granted JPS5815012A (en) 1981-07-22 1981-07-22 Manufacture of cubic system boron nitride

Country Status (1)

Country Link
JP (1) JPS5815012A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6077110A (en) * 1983-10-05 1985-05-01 Showa Denko Kk Synthesis of cubic boron nitride
JPS62108717A (en) * 1985-11-07 1987-05-20 Denki Kagaku Kogyo Kk Production of cubic boron nitride

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6077110A (en) * 1983-10-05 1985-05-01 Showa Denko Kk Synthesis of cubic boron nitride
JPH0593B2 (en) * 1983-10-05 1993-01-05 Showa Denko Kk
JPS62108717A (en) * 1985-11-07 1987-05-20 Denki Kagaku Kogyo Kk Production of cubic boron nitride

Also Published As

Publication number Publication date
JPS6366254B2 (en) 1988-12-20

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