JPH08189B2 - Method for producing cubic boron nitride - Google Patents
Method for producing cubic boron nitrideInfo
- Publication number
- JPH08189B2 JPH08189B2 JP1201416A JP20141689A JPH08189B2 JP H08189 B2 JPH08189 B2 JP H08189B2 JP 1201416 A JP1201416 A JP 1201416A JP 20141689 A JP20141689 A JP 20141689A JP H08189 B2 JPH08189 B2 JP H08189B2
- Authority
- JP
- Japan
- Prior art keywords
- cbn
- boron nitride
- pressure
- rbn
- temperature
- 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.)
- Expired - Fee Related
Links
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 title claims description 29
- 229910052582 BN Inorganic materials 0.000 title claims description 28
- 238000004519 manufacturing process Methods 0.000 title claims description 10
- 239000000843 powder Substances 0.000 claims description 14
- 239000003054 catalyst Substances 0.000 claims description 11
- 230000003068 static effect Effects 0.000 claims description 5
- 239000011812 mixed powder Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 10
- 239000002245 particle Substances 0.000 description 10
- 238000009792 diffusion process Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000007704 transition Effects 0.000 description 5
- 239000013078 crystal Substances 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 229910052796 boron Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 230000017525 heat dissipation Effects 0.000 description 2
- LELOWRISYMNNSU-UHFFFAOYSA-N hydrogen cyanide Chemical compound N#C LELOWRISYMNNSU-UHFFFAOYSA-N 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 230000000737 periodic effect Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000000758 substrate Substances 0.000 description 2
- 239000006061 abrasive grain Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 150000001639 boron compounds Chemical class 0.000 description 1
- 229910052810 boron oxide Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000011088 calibration curve Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 229910003460 diamond Inorganic materials 0.000 description 1
- 239000010432 diamond Substances 0.000 description 1
- JKWMSGQKBLHBQQ-UHFFFAOYSA-N diboron trioxide Chemical compound O=BOB=O JKWMSGQKBLHBQQ-UHFFFAOYSA-N 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 239000000411 inducer Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000003754 machining Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005121 nitriding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000009931 pascalization Methods 0.000 description 1
- 238000000634 powder X-ray diffraction Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000004065 semiconductor Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229910052984 zinc sulfide Inorganic materials 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J3/00—Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
- B01J3/06—Processes using ultra-high pressure, e.g. for the formation of diamonds; Apparatus therefor, e.g. moulds or dies
- B01J3/062—Processes using ultra-high pressure, e.g. for the formation of diamonds; Apparatus therefor, e.g. moulds or dies characterised by the composition of the materials to be processed
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2203/00—Processes utilising sub- or super atmospheric pressure
- B01J2203/06—High pressure synthesis
- B01J2203/0605—Composition of the material to be processed
- B01J2203/0645—Boronitrides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2203/00—Processes utilising sub- or super atmospheric pressure
- B01J2203/06—High pressure synthesis
- B01J2203/065—Composition of the material produced
- B01J2203/066—Boronitrides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Ceramic Products (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 窒化ほう素の高圧相である立方晶窒化ほう素(以下
「cBN」で示す)は、ダイヤモンドに次ぐ硬さと熱伝導
率を有し、また化学的に安定であることから、鉄系金属
の機械加工用工具や半導体デバイスの放熱基板としての
利用が進められている。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) Cubic boron nitride (hereinafter referred to as “cBN”), which is a high-pressure phase of boron nitride, has hardness and thermal conductivity second only to diamond, and Since it is chemically stable, it is being used as a tool for machining iron-based metals and as a heat dissipation substrate for semiconductor devices.
本発明は、低圧相窒化ほう素から触媒を用いない静的
高温高圧法によってcBNを得るための製造方法に関する
ものである。The present invention relates to a production method for obtaining cBN from low pressure phase boron nitride by a static high temperature high pressure method without using a catalyst.
(従来の技術) 一般にcBNは、窒化ほう素の低圧相である六方晶BN
(以下「hBN」で示す)もしくは乱層構造BN(以下「tB
N」で示す)をcBNの熱力学安定条件下に保持することに
よって得られる。cBNの熱力学安定条件を得る方法とし
て、静的高圧高温処理を用いる場合には転換圧力と温度
条件を例えば65kbar、2100℃以上の非常に厳しい条件が
要求される。そのため、工業的には触媒を用いて転換条
件を40〜50kbar、1500℃程度の比較的穏やかな条件とす
ることが行われている。この方法により単結晶型のcBN
粒子が生成され、そのまま砥石などの研削工具の砥粒と
して用いられている。(Prior Art) Generally, cBN is hexagonal BN, which is a low-pressure phase of boron nitride.
(Hereinafter referred to as “hBN”) or turbostratic structure BN (hereinafter referred to as “tB”).
(Denoted by "N") is maintained under thermodynamically stable conditions for cBN. When using static high-pressure and high-temperature treatment as a method for obtaining the thermodynamic stability condition of cBN, very severe conditions such as conversion pressure and temperature conditions of 65 kbar and 2100 ° C or higher are required. Therefore, industrially, a catalyst is used to set the conversion conditions to 40 to 50 kbar and a relatively mild condition of about 1500 ° C. By this method, single crystal type cBN
Particles are generated and used as they are as abrasive grains for a grinding tool such as a grindstone.
一方、微細なcBN粒子を高圧、高温下に焼結すると切
削工具用焼結体が得られるが、cBNは単体では焼結しに
くいため金属やセラミックスなどの結合助剤と混合して
焼結する必要がある。現在工業的に利用されているcBN
はそのほとんどが上述の方法で製造されているところ、
触媒の取り込みおよび焼結助剤の存在がcBN本来の特性
を低下させるという欠点があり、このため触媒および焼
結助剤を用いない無触媒直接転換法(以下、「直接法」
という)により、cBNの粒子および焼結体の製造を、よ
り穏やかな条件下に実現することが望まれている。直接
法によるcBNは微細粒子から構成された多結晶体であ
り、高硬度、高純度、光熱伝導性、高靭性などの特長を
有するので、工具材料、放熱基板として優れた性能を発
揮するものと期待されるからである。On the other hand, when fine cBN particles are sintered under high pressure and high temperature, a sintered body for cutting tools can be obtained, but cBN is difficult to sinter alone, so it is mixed with a bonding aid such as metal or ceramics and sintered. There is a need. CBN currently used industrially
Where most of them are manufactured by the above method,
The disadvantage is that the incorporation of catalyst and the presence of sintering aid deteriorates the original properties of cBN. Therefore, the catalyst-free direct conversion method without using catalyst and sintering aid (hereinafter referred to as "direct method").
Therefore, it is desired to realize the production of cBN particles and sintered bodies under milder conditions. CBN produced by the direct method is a polycrystalline body composed of fine particles and has features such as high hardness, high purity, photothermal conductivity, and high toughness, so it is expected to exhibit excellent performance as a tool material and heat dissipation substrate. Because it is expected.
直接法によるcBNの製造法としては次の文献が従来既
知である。The following documents are conventionally known as methods for producing cBN by the direct method.
文献1)マテリアルズ・リサーチ・ブルチン(Material
s Research Bulletin),7,999−1004(1972) 文献2)特開昭54−33510号公報 文献1)には、低結晶性の窒化ほう素を出発原料として
1250℃以上の温度および60kbar以上の圧力で処理するこ
とにより「ランプ(lump)」状cBNが得られたことが示
されている。しかし、この例ではH2Oが触媒として作用
した可能性が指摘され(福長脩「立方晶窒化ほう素の合
成と応用」、セラミックデータブック′85,431−436(1
985)参照)、また追試例もなく、不明な点が多い。Reference 1) Materials Research Burchin (Material)
s Research Bulletin), 7,999-1004 (1972) Reference 2) JP-A-54-33510 Reference 1) uses low crystalline boron nitride as a starting material.
It has been shown that "lump" cBN was obtained by processing at temperatures above 1250 ° C and pressures above 60 kbar. However, in this example, it was pointed out that H 2 O acted as a catalyst (Shun Fukunaga, "Synthesis and Application of Cubic Boron Nitride", Ceramic Data Book '85, 431-436 (1
985))), and there are no additional trials, and there are many unclear points.
文献2)には、熱分解窒化ほう素の成型体を1800℃以
上の温度および50kbar以上の圧力で高温高圧処理して、
cBN焼結体を製造することが開示されている。Reference 2) describes that a molded body of pyrolytic boron nitride is subjected to high temperature and high pressure treatment at a temperature of 1800 ° C. or higher and a pressure of 50 kbar or higher,
It is disclosed to produce a cBN sintered body.
この他にも触媒を使用せずに静的高温高圧処理でcBN
を製造する報告は数例あるが、それらはいずれも、1800
℃以上の温度と60kbar以上の圧力といった厳しい条件下
での高温高圧処理が必要であり、工業的生産には不適当
である。Besides this, cBN can be treated by static high temperature and high pressure treatment without using a catalyst.
There are several reports of manufacturing
It requires high temperature and high pressure treatment under severe conditions such as temperature above ℃ and pressure above 60 kbar, which is not suitable for industrial production.
一方、他の立方晶窒化ほう素の製造法と題して、特公
昭60−2245号公報には、原料として菱面体窒化ほう素
(rBN)を用い室温下、衝撃波加圧でcBNを得る方法が開
示されているが、文中に述べられているように逆転換を
抑えるためには放熱材として金属粉を80重量%以上も加
える必要があり、生産効率が非常に悪いばかりか、cBN
単一成分からなる焼結体を得ることもできず、この放熱
材の配合がcBN本来の特性を低下させるという欠点を持
っている。また、cBN中にウルツ鉱型の窒化ほう素を副
生させないためには、原料としてrBNのみからなる低圧
相窒化ほう素を用いる必要がある。しかし、rBNは特殊
な条件下においてのみその合成が可能な低圧相窒化ほう
素であるため、高価でその入手が困難でありrBNのみか
らなる低圧相窒化ほう素を用いることには多くの問題点
があった。On the other hand, as another method for producing cubic boron nitride, Japanese Patent Publication No. 60-2245 discloses a method for obtaining cBN by shock wave pressurization at room temperature using rhombohedral boron nitride (rBN) as a raw material. Although disclosed, as described in the text, it is necessary to add 80% by weight or more of metal powder as a heat radiating material in order to suppress the reverse conversion, and not only the production efficiency is very poor, but also cBN
It is not possible to obtain a sintered body consisting of a single component, and the compounding of this heat-dissipating material has the drawback of degrading the original properties of cBN. Further, in order to prevent wurtzite type boron nitride from being produced as a by-product in cBN, it is necessary to use low-pressure phase boron nitride composed only of rBN as a raw material. However, since rBN is a low-pressure phase boron nitride that can be synthesized only under special conditions, it is expensive and difficult to obtain, and there are many problems in using low-pressure phase boron nitride consisting only of rBN. was there.
(発明が解決しようとする課題) 直接法によるcBNの合成を従来よりも低温・低圧の条
件下に可能ならしめ、工業的生産性が低いためにこれま
で実用化が困難であった高純度のcBNの粒子またはその
焼結体を得ることが本発明の目的である。(Problems to be solved by the invention) Since the synthesis of cBN by the direct method can be performed under the condition of lower temperature and lower pressure than the conventional method, it has been difficult to put it to practical use because of its low industrial productivity. It is an object of the present invention to obtain particles of cBN or a sintered body thereof.
発明者らは直接法によるcBNの製造方法、特に原料と
して使用する低圧相窒化ほう素の種類とcBNへの転換条
件との関係について種々検討した結果、従来の原料に少
量のrBNを、hBN粉末がcBNに転換するための誘発・促進
剤として加えたものを用いることにより、意外にも従来
より著しく穏やかな高温高圧条件下にcBNへの転換が可
能となることを見いだし、本発明に至ったものである。The inventors have conducted various studies on the method for producing cBN by the direct method, particularly the relationship between the type of low-pressure phase boron nitride used as a raw material and the conversion conditions to cBN, and as a result, a small amount of rBN in the conventional raw material, hBN powder. However, by using the one added as an inducer / promoter for converting into cBN, it was unexpectedly found that the conversion into cBN is possible under a condition of mildly high temperature and high pressure, which led to the present invention. It is a thing.
(課題を解決するための手段) すなわち、本発明は低圧相室化ほう素を、触媒を使用
せず静的超高圧高温で処理して立方晶窒化ほう素を製造
するにあたり、低圧相窒化ほう素が六方晶窒化ほう素
(hBN)粉末99〜60重量%と菱面体窒化ほう素(rBN)粉
末1〜40重量%の混合粉末の成形体であることを特徴と
する立方晶窒化ほう素の製造方法である。(Means for Solving the Problems) That is, according to the present invention, low-pressure phase nitriding boron is used for producing cubic boron nitride by treating low-pressure phase-chambered boron at a static ultrahigh pressure and high temperature without using a catalyst. Of cubic boron nitride, characterized in that the element is a compact of a mixed powder of 99 to 60% by weight of hexagonal boron nitride (hBN) powder and 1 to 40% by weight of rhombohedral boron nitride (rBN) powder. It is a manufacturing method.
以下、さらに詳しく本発明について説明する。 The present invention will be described in more detail below.
本発明において原料として使用する低圧相窒化ほう素
はhBN粒子にrBN粒子を加え混合した成形体である。The low-pressure phase boron nitride used as a raw material in the present invention is a compact obtained by adding and mixing rBN particles to hBN particles.
ここにhBN粒子は工業的に広く生産されている物質で
あり、容易に入手することができる。Here, hBN particles are industrially widely produced substances and can be easily obtained.
一方、rBN粒子は例えば特公昭60−2244号公報に記載
されているように酸素を含むほう素化合物とシアンガス
との反応により合成することができる。On the other hand, rBN particles can be synthesized by the reaction of a boron compound containing oxygen and cyan gas as described in, for example, Japanese Patent Publication No. 60-2244.
本発明で用いる低圧窒化ほう素のrBN含有率は1〜40
%が適当である。rBNの含有率1%未満では、原料全体
をcBNに転換するのに長時間を要するため、その効果が
ほとんどなく、またその含有率を大きくすると前述した
ように他の低圧窒化ほう素に較べ入手が困難なrBNを多
く必要とすることから経済性が低下する。The low-pressure boron nitride used in the present invention has an rBN content of 1 to 40.
% Is appropriate. If the content of rBN is less than 1%, it takes a long time to convert the entire raw material into cBN, so that the effect is almost nonexistent, and if the content is increased, it can be obtained compared to other low-pressure boron nitride. Since it requires a large amount of rBN, which is difficult to achieve, economic efficiency is reduced.
本発明方法に係わる以上の原料は粉末の成形体に加工
され、ベルト型高温発生装置に装填される。その後、ま
ず圧力を続いて温度を上昇させ、所望の温度・圧力で一
定時間保持して高温高圧処理を行う。この際、保持する
温度、圧力および時間は、好ましくはそれぞれ1700〜20
50℃、50〜65kbarおよび5分−3時間である。処理後は
まず温度を、続いて圧力をそれぞれ室温および1気圧ま
で戻し、装置内から高温高圧処理で製造されたcBNを取
り出す。得られたcBNは従来の触媒を使用せずに製造さ
れたcBNと同様の優れた特性を持っており、本発明によ
り従来に較べて生産性の高い穏やかな高温高圧条件下で
優れた特性を持つcBNの製造を行うことができる。The above raw materials according to the method of the present invention are processed into powder compacts and loaded into a belt type high temperature generator. After that, first, the pressure is subsequently raised, and the temperature and pressure are maintained at a desired temperature and pressure for a certain period of time to perform high temperature and high pressure processing. At this time, the temperature, pressure and time to be held are preferably 1700 to 20 respectively.
50 ° C., 50-65 kbar and 5 minutes-3 hours. After the treatment, first the temperature and then the pressure are returned to room temperature and 1 atm, respectively, and cBN produced by the high temperature and high pressure treatment is taken out of the apparatus. The obtained cBN has the same excellent properties as cBN produced without using a conventional catalyst, and the present invention provides excellent properties under mild high temperature and high pressure conditions with higher productivity than the conventional one. It is possible to manufacture the own cBN.
(作 用) 従来、cBNの原料として用いられる低圧相窒化ほう素
は、入手の容易さや価格の面からhBN及び/又はtBNが広
く使われた。しかし、これら従来の原料では例えば文献
2)の実施例のように、温度2100℃以上および圧力65kb
ar以上のように厳しい高温高圧処理が必要であって工業
生産に適さない。しかし、この従来原料に前述した方法
で少量のrBNを含ませた本発明の原料を用いると、例え
ば1700〜2050℃および50〜65kbarの生産性に優れた温度
圧力条件で触媒を使用せずにcBNの製造が可能となる。(Working) Conventionally, hBN and / or tBN has been widely used as the low-pressure phase boron nitride used as a raw material of cBN because of its availability and price. However, these conventional raw materials have a temperature of 2100 ° C. or higher and a pressure of 65 kb as in the example of Reference 2).
It is not suitable for industrial production because it requires severe high-temperature and high-pressure treatment as above. However, when the raw material of the present invention containing a small amount of rBN in the above-mentioned conventional raw material is used, for example, 1700 to 2050 ° C. and 50 to 65 kbar without using a catalyst under excellent temperature and pressure conditions for productivity. cBN can be manufactured.
このような穏やかな条件でcBNへの直接転換が可能に
なるのは次のような理由によると思われる。The reason why the direct conversion to cBN is possible under such mild conditions is considered to be as follows.
本発明の原料はhBN粉末99〜60重量%とrBN粉末1〜40
重量%の混合粉末の成形体よりなる。The raw materials of the present invention are 99 to 60% by weight of hBN powder and 1 to 40 of rBN powder.
It consists of a compact of a powder mixture of weight%.
ここにrBNは、hBNとは異なる結晶構造を持つ。 Here, rBN has a different crystal structure from hBN.
すなわち、hBNはほう素と窒素が交互に結合して形成
される六角網目層の積み重なりの周期がABABAB……の二
層周期であり、また、rBNはその周期がABCABCABC……の
三層周期である。In other words, hBN is a two-layer cycle in which the stacking period of hexagonal network layers formed by alternating bonding of boron and nitrogen is ABABAB ……, and rBN is a three-layer cycle in which the cycle is ABCABCABC ……. is there.
cBNは、<111>方向から見れば積層の周期はrBNと同
じABCABCABC……の三層周期を持ち、このような結晶構
造の類似性からrBNの六角網目層の層間を圧縮し、六角
網目を構成する原子を交互にその平面から少し移動させ
ることによってcBNの構造に転換することが可能と考え
られる。When viewed from the <111> direction, cBN has a three-layer cycle of ABCCABCABC ..., which is the same as rBN. Due to the similar crystal structure, the layers of the hexagonal network layer of rBN are compressed to form a hexagonal network. It is thought that it is possible to convert to the structure of cBN by moving the constituent atoms alternately a little from the plane.
この転換はBN構成原子相互の位置の入れ換えなしに起
こるいわゆる無拡散転移である。This conversion is a so-called non-diffusion transition that occurs without changing the positions of BN constituent atoms.
これに対しhBNをcBNに転換しようとすれば、二層周期
の積層構造をくずし、三層周期の積層構造に変えるいわ
ゆる拡散転移過程が必要である。On the other hand, if hBN is to be converted to cBN, a so-called diffusion transition process is required to break the two-layer periodic structure into a three-layer periodic structure.
一般に、無拡散転移は拡散転移に較べ容易にまた短時
間に起こると考えられる。Generally, the non-diffusion transition is considered to occur more easily and in a shorter time than the diffusion transition.
本発明の原料を1700〜2050℃および5〜6.5万気圧の
条件で高温高圧処理した場合、まずrBNが短時間の内に
無拡散転移によりcBNに転換すると考えられる。次に、
同条件下ではそれ単一では転換を起こさないhBNもすで
に転換しそれに接しているcBN粒子の成長に伴ってその
中に取り込まれてcBNに転換して、最終的には原料全体
がcBNに転換するものと思われる。When the raw material of the present invention is subjected to high temperature and high pressure treatment under the conditions of 1,700 to 20,050 ° C. and 5 to 65,000 atm, it is considered that rBN is first converted to cBN by a non-diffusion transition within a short time. next,
Under the same conditions, hBN, which does not cause conversion by itself, has already converted, and it is taken into and converted into cBN as the cBN particles in contact therewith grow, and eventually the entire raw material changes to cBN. It seems to do.
(実施例) 次に、本発明を実施例と比較例をあげた表1に基いて
さらに具体的に説明する。(Example) Next, the present invention will be described more specifically based on Table 1 showing Examples and Comparative Examples.
実施例1−12 特公昭60−2244号公報に開示の方法で、気化させた酸
化ほう素にシアン化水素を反応させ、太さ約1ミクロン
のrBNの針状結晶を合成した。このrBNウィスカーを粉砕
し、市販のhBN粉末に対し表1に示す比率となるように
混合した。 Example 1-12 According to the method disclosed in Japanese Patent Publication No. 60-2244, hydrogen cyanide was reacted with vaporized boron oxide to synthesize acicular crystals of rBN having a thickness of about 1 micron. The rBN whiskers were crushed and mixed with a commercially available hBN powder in the ratio shown in Table 1.
これらの混合粉末を加圧成形し、円板を得てベルト型
高温高圧発生装置を用いて表1に示す温度、圧力条件に
て所定の時間、高温高圧処理を行った。These mixed powders were pressure-molded to obtain a disk, which was subjected to a high-temperature high-pressure treatment for a predetermined time under the temperature and pressure conditions shown in Table 1 using a belt-type high-temperature high-pressure generator.
処理後の試料について粉末X線回折測定を行い、試料
中のcBNの重量%を、あらかじめ作製しておいた検量線
から求め表1に掲げた。Powder X-ray diffraction measurement was performed on the treated sample, and the weight% of cBN in the sample was determined from the calibration curve prepared in advance and is listed in Table 1.
比較例1−12 cBNの原料として市販のhBNのみからなる粉末を成形し
た円板を用いた以外は、実施例1−12と同様な条件で実
施した。Comparative Example 1-12 Example 1-12 was carried out under the same conditions as Example 1-12, except that a disk formed by molding powder consisting of only hBN was used as a raw material of cBN.
(発明の効果) 本発明によれば、触媒を用いない直接法によるcBNの
合成を、hBN粉末99〜60重量%とrBN粉末1〜40重量%の
混合粉末成形体を原料として準備し、これを原料とする
ことにより、従来よりも著しく穏やかな高温高圧条件下
で実現できるため、今までは工業的生産性が低いために
実用化されていなかった高純度のcBNの粒子またはその
焼結体を得ることができるという効果がある。(Effect of the invention) According to the present invention, the synthesis of cBN by a direct method without a catalyst is prepared by using a mixed powder compact of 99-60 wt% hBN powder and 1-40 wt% rBN powder as a raw material. Since it can be realized under high temperature and high pressure conditions, which is significantly milder than before, by using as a raw material, high-purity cBN particles or a sintered body thereof that has not been put into practical use due to low industrial productivity up to now. There is an effect that can be obtained.
フロントページの続き (56)参考文献 特開 昭61−31359(JP,A) 特開 平1−184033(JP,A) 特公 昭64−3948(JP,B2)Continuation of the front page (56) References JP-A-61-31359 (JP, A) JP-A-1-184033 (JP, A) JP-B 64-3948 (JP, B2)
Claims (1)
超高圧高温で処理して立方晶窒化ほう素を製造するにあ
たり、低圧相窒化ほう素が六方晶窒化ほう素(hBN)粉
末99〜60重量%と菱面体窒化ほう素(rBN)粉末1〜40
重量%の混合粉末の成形体であることを特徴とする立方
晶窒化ほう素の製造方法。1. A low-pressure phase boron nitride is a hexagonal boron nitride (hBN) when a low-pressure phase boron nitride is processed at a static ultrahigh pressure and high temperature without using a catalyst to produce cubic boron nitride. Powder 99-60% by weight and rhombohedral boron nitride (rBN) powder 1-40
A method for producing cubic boron nitride, which is a compact of a mixed powder of wt%.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1201416A JPH08189B2 (en) | 1989-08-04 | 1989-08-04 | Method for producing cubic boron nitride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1201416A JPH08189B2 (en) | 1989-08-04 | 1989-08-04 | Method for producing cubic boron nitride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0365234A JPH0365234A (en) | 1991-03-20 |
| JPH08189B2 true JPH08189B2 (en) | 1996-01-10 |
Family
ID=16440722
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1201416A Expired - Fee Related JPH08189B2 (en) | 1989-08-04 | 1989-08-04 | Method for producing cubic boron nitride |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08189B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2001036081A1 (en) * | 1999-11-19 | 2001-05-25 | De Beers Industrial Diamonds (Proprietary) Limited | Cubic boron nitride clusters |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61223183A (en) * | 1985-03-04 | 1986-10-03 | Res Dev Corp Of Japan | Production of rhombohedral system boron nitride |
| JPH01184033A (en) * | 1988-01-19 | 1989-07-21 | Natl Inst For Res In Inorg Mater | Production of cubic boron nitride |
-
1989
- 1989-08-04 JP JP1201416A patent/JPH08189B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0365234A (en) | 1991-03-20 |
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