JPH0815548B2 - Method for synthesizing cubic boron nitride - Google Patents
Method for synthesizing cubic boron nitrideInfo
- Publication number
- JPH0815548B2 JPH0815548B2 JP62327295A JP32729587A JPH0815548B2 JP H0815548 B2 JPH0815548 B2 JP H0815548B2 JP 62327295 A JP62327295 A JP 62327295A JP 32729587 A JP32729587 A JP 32729587A JP H0815548 B2 JPH0815548 B2 JP H0815548B2
- Authority
- JP
- Japan
- Prior art keywords
- hbn
- cbn
- boron nitride
- weight
- catalyst
- 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
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
-
- 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
- B01J2203/0675—Structural or physico-chemical features of the materials processed
- B01J2203/068—Crystal growth
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 本発明は立方晶窒化硼素(以下CBNという)の合成方
法に関し、特に良晶のCBNをより低圧、低温で得ること
のできる合成方法に関するものである。Description: TECHNICAL FIELD The present invention relates to a method for synthesizing cubic boron nitride (hereinafter referred to as CBN), and particularly to a method for synthesizing good-crystal CBN at a lower pressure and a lower temperature. .
従来の技術 従来、CBN合成に使用される原料の六方晶窒化硼素
(以下HBNという)は一般に市販品で結晶が十分発達し
たX線によるC軸方向の結晶の大きさLcが1000Å以上の
ものが使用されている。それは低結晶性でLc値が1000Å
以下のHBNは通常B2O3等の不純物が5%程度含有されて
おり、このB2O3不純物はCBNの成長を多いに阻害し、か
つ良結晶が得られないからである。Conventional technology Conventionally, a hexagonal boron nitride (hereinafter referred to as HBN), which is a raw material used for CBN synthesis, is generally a commercially available product with a fully developed crystal and a crystal size Lc in the C-axis direction of X-rays of 1000 Å or more. in use. It has low crystallinity and Lc value of 1000Å
The following HBN are impurities such as normal B 2 O 3 is contained about 5%, the B 2 O 3 impurities is inhibited in many cases the CBN growth, and good because crystals can not be obtained.
発明が解決しようとする問題点 CBNの合成に結晶が一様に発達したHBNを用いるとCBN
安定域で加圧、加熱した場合、HBNがCBN合成触媒に同時
に溶解し、CBNの成長が開始されるため、特に成長初期
に骸晶の形になり、それ以後の成長がランダムになり、
最終的に出来た結晶は表面に凹凸が出来たり、内部に気
孔をもったような結晶が得られる場合がある。このこと
は低結晶性HBN中のB2O3などの不純物を除いたものを用
いた場合も同様である。Problems to be Solved by the Invention If HBN with uniformly developed crystals is used for the synthesis of CBN, CBN
When pressurized and heated in the stable region, HBN is simultaneously dissolved in the CBN synthesis catalyst, and the growth of CBN is started, so that it becomes a skeletal form especially at the early stage of growth, and the growth thereafter becomes random,
The finally formed crystals may have irregularities on the surface or may have crystals having pores inside. This also applies to the case where impurities such as B 2 O 3 in low crystalline HBN are removed.
本発明の目的はこのような結晶のよいCBNの合成方法
を提供し、さらには合成の温度や圧力を従来より下げて
もCBNの合成が可能な方法を提供することにある。An object of the present invention is to provide a method for synthesizing CBN having such a good crystal, and further to provide a method for synthesizing CBN even if the temperature and pressure for synthesis are lowered as compared with the conventional method.
問題点を解決するための手段 CBNの成長を合成の初期から最後まで制御する方法と
しては圧力、温度をCBN−HBNの平衡線近傍で合成する方
法であるが、試料空間内には圧力、温度のバラツキが避
けられず、そのために試料空間全体を良晶生成の圧力、
温度に保持することは非常に困難である。Means to solve the problem As a method to control the growth of CBN from the beginning to the end of synthesis, there is a method of synthesizing pressure and temperature near the equilibrium line of CBN-HBN, but in the sample space, pressure and temperature Is inevitable, and for that reason, the pressure for forming good crystals in the entire sample space,
Maintaining temperature is very difficult.
本発明者はCBN合成触媒へのHBNの溶解速度がHBNの結
晶化度に基因することを見出した。結晶が未発達のHBN
(Lc値が1000Å未満)は結晶学的に不安定であり、触媒
への溶解が早い。またこのようなHBNは一般的に粒子の
大きさも小さく、表面積が大きいため触媒との接触面積
が大きいため触媒との接触面積が相対的に多くなり溶解
が早い。The present inventor has found that the dissolution rate of HBN in the CBN synthesis catalyst is based on the crystallinity of HBN. HBN with undeveloped crystals
(Lc value less than 1000Å) is crystallographically unstable and dissolves quickly in the catalyst. In addition, such HBN generally has a small particle size, a large surface area, and a large contact area with the catalyst, so that the contact area with the catalyst is relatively large and the HBN dissolves quickly.
そこで本発明はこの結晶化度の低いHBNを結晶化度の
高いHBNに混合することにより、溶解を段階的に行なう
ようにしたものである。Therefore, in the present invention, the HBN having a low degree of crystallinity is mixed with the HBN having a high degree of crystallinity to carry out the dissolution stepwise.
即ち、本発明はCBN合成触媒の存在下にHBNよりCBNを
合成する際にX線による結晶化度Lcが1000Å以上のHBN
粉末30〜90重量%とLcが1000Å未満のHBN粉末70〜10重
量%とを混合したものを原料として用い、熱力学的にCB
Nの安定域に加熱、加圧することを特徴とするCBNの合成
方法である。That is, according to the present invention, when synthesizing CBN from HBN in the presence of a CBN synthesizing catalyst, HBN having a crystallinity Lc of 1000 Å or more by X-ray is used.
Using a mixture of 30 to 90% by weight of powder and 70 to 10% by weight of HBN powder having an Lc of less than 1000Å as a raw material, thermodynamically CB
It is a method for synthesizing CBN which is characterized by heating and pressurizing to a stable region of N.
Lcが1000Å以上のHBNは市販されているのでそのまま
用いることができる。その粉末の粒度は30μm以下が望
ましい。この市販のHBNはB2O3等を原料にして製造され
た後高温で熱処理されたものである。Lcが1000Å未満の
HBNは上記の熱処理をしないか或いは熱処理温度を低く
して得ることができる。通常はこのHBNにはB2O3等の不
純物がかなり含まれているので、水洗、酸洗等で不純物
を除去する。これを乾燥し、粉末とする。必要によって
はさらに粉砕する。粉末の粒度は5μm以下が望まし
い。HBN with Lc of 1000Å or more is commercially available and can be used as it is. The particle size of the powder is preferably 30 μm or less. This commercially available HBN is manufactured by using B 2 O 3 or the like as a raw material and then heat-treated at a high temperature. Lc less than 1000Å
HBN can be obtained without the above heat treatment or at a low heat treatment temperature. Usually, this HBN contains a considerable amount of impurities such as B 2 O 3, so impurities are removed by washing with water or pickling. This is dried and made into powder. Grind further if necessary. The particle size of the powder is preferably 5 μm or less.
結晶化度の高いHBNと低いHBNの混合割合は前記した通
りであるが、これはHBNが一度に合成触媒に溶解するこ
とを避けるため必要である。The mixing ratio of HBN having a high degree of crystallinity and HBN having a low degree of crystallinity is as described above, but this is necessary in order to prevent HBN from being dissolved in the synthesis catalyst at once.
CBN合成触媒は通常使用されるもの、即ち、アルカリ
金属、アルカリ土類金属、これらの窒化物等で具体的に
はLi,Na,Ca,Sr,Li3N,Ca3N2,Li3BN2,LiBaBN2等が用いら
れる。これらのHBNに対する混合割合はHBN100重量部に
対し、触媒1〜30重量部が一般的である。CBN synthesis catalysts are commonly used, that is, alkali metals, alkaline earth metals, nitrides of these, specifically, Li, Na, Ca, Sr, Li 3 N, Ca 3 N 2 , Li 3 BN. 2 , LiBaBN 2 and the like are used. The mixing ratio of these to HBN is generally 1 to 30 parts by weight of catalyst to 100 parts by weight of HBN.
CBNの合成はこれらの混合粉末を予備成形し、超高圧
装置に装填して行なわれる。CBN is synthesized by preforming these mixed powders and loading them into an ultrahigh pressure device.
合成条件は通常の条件より低温、低圧でも可能であ
り、例えば1400℃〜1700℃,40kb〜50kbが適当である。The synthesis conditions may be lower than usual conditions and low pressure, for example, 1400 ° C to 1700 ° C, 40 kb to 50 kb are suitable.
作 用 結晶化度の高いHBNに結晶化度のHBNを混合することに
より、CBN合成において、先ず結晶化度の低いHBNが触媒
に溶解し、CBNが生成する。次に結晶化度の高いCBNが溶
解し、先に生成したCBNの表面でCBNとなって析出し、粒
の成長が起こると考えられる。By mixing HBN with high crystallinity with HBN with high crystallinity, in the synthesis of CBN, HBN with low crystallinity is first dissolved in the catalyst to form CBN. It is considered that CBN having a high degree of crystallinity then melts and precipitates as CBN on the surface of the previously produced CBN, causing grain growth.
実施例 市販のHBN(Lc値が1000Å以上、粒度30μm以下)50
重量%と結晶性の低いHBN(Lc値が250Å,粒度5μm以
下,純度99重量%以上)50重量%を混合し、その混合物
100重量部に対し、触媒としてLiCaBN2を10重量部を混合
し、冷間で成形した後50kb,1500℃,10分間加圧、加熱処
理をした。得られたCBNは自形をもち透明感のある結晶
であった。Example Commercially available HBN (Lc value of 1000Å or more, particle size of 30 μm or less) 50
% By weight and 50% by weight of HBN with low crystallinity (Lc value of 250Å, particle size of 5 μm or less, purity of 99% by weight or more), and the mixture
10 parts by weight of LiCaBN 2 as a catalyst was mixed with 100 parts by weight, cold-molded, and then subjected to heat treatment at 50 kb and 1500 ° C. for 10 minutes. The obtained CBN was a transparent crystal with an automorphic shape.
比較例1 上と同じHBN(Lc値が1000Å以上)100重量部に対し、
触媒としてLiCaBN2を10重量部を混合し1)と同じ条件
でCBNを合成したところ、得られたCBNは表面に凹凸が見
られ、かつ内部に失透した部分のあるものであった。Comparative Example 1 For 100 parts by weight of the same HBN (Lc value of 1000Å or more) as above,
When 10 parts by weight of LiCaBN 2 was mixed as a catalyst and CBN was synthesized under the same conditions as in 1), the obtained CBN had irregularities on the surface and a devitrified portion inside.
比較例2 Lcが250ÅのHBN(純度90%<)100重量部に対し、触
媒としてLiCaBN2を10重量部混合し、実施例と同じ条件
でCBNを合成したところ、自形がなく破砕した粒がほと
んどであり、透明感もなかった。Comparative Example 2 100 parts by weight of HBN (purity 90% <) having Lc of 250 Å was mixed with 10 parts by weight of LiCaBN 2 as a catalyst, and CBN was synthesized under the same conditions as in Example. Most of them were not transparent.
発明の効果 本発明によればCBNの合成において触媒へのHBNの溶解
速度をそのHBNの結晶化度により制御出来るため、成長
初期から最後までほぼ一定の速度で成長させることが出
来、良晶を得ることが出来る。EFFECTS OF THE INVENTION According to the present invention, in the synthesis of CBN, the dissolution rate of HBN in the catalyst can be controlled by the crystallinity of the HBN, so that it can be grown at a substantially constant rate from the initial growth to the end, and a good crystal is formed. You can get it.
Claims (1)
方晶窒化硼素粉末30〜90重量%とLcが1000Å未満の六方
晶窒化硼素粉末70〜10重量%とを混合し、これに立方晶
窒化硼素の合成触媒を加え、熱力学的に立方晶窒化硼素
の安定域で加圧、加熱することを特徴とする立方晶窒化
硼素の合成方法。1. A mixture of 30 to 90% by weight of hexagonal boron nitride powder having a crystallinity of Lc of X-ray index of 1000Å or more and 70 to 10% by weight of hexagonal boron nitride powder having an Lc of less than 1000Å. A method for synthesizing cubic boron nitride, comprising adding a catalyst for synthesizing cubic boron nitride to, and thermodynamically pressurizing and heating in a stable region of cubic boron nitride.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62327295A JPH0815548B2 (en) | 1987-12-25 | 1987-12-25 | Method for synthesizing cubic boron nitride |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP62327295A JPH0815548B2 (en) | 1987-12-25 | 1987-12-25 | Method for synthesizing cubic boron nitride |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01168328A JPH01168328A (en) | 1989-07-03 |
| JPH0815548B2 true JPH0815548B2 (en) | 1996-02-21 |
Family
ID=18197532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP62327295A Expired - Fee Related JPH0815548B2 (en) | 1987-12-25 | 1987-12-25 | Method for synthesizing cubic boron nitride |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0815548B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7214359B2 (en) * | 2003-02-03 | 2007-05-08 | Showa Denko K.K. | Cubic boron nitride, catalyst for synthesizing cubic boron nitride, and method for producing cubic boron nitride |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5858383B2 (en) * | 1975-07-31 | 1983-12-24 | 松下電工株式会社 | Mushitsuketsugozai |
| JPS60195007A (en) * | 1984-03-14 | 1985-10-03 | Komatsu Ltd | Synthesis method of cubic boron nitride |
-
1987
- 1987-12-25 JP JP62327295A patent/JPH0815548B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01168328A (en) | 1989-07-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4016244A (en) | Process for production of cubic boron nitride | |
| JPS595547B2 (en) | Method for manufacturing cubic boron nitride sintered body | |
| US3772428A (en) | Continuous growth of cubic boron nitride | |
| US6984448B1 (en) | Cubic boron nitride clusters | |
| JPH0815548B2 (en) | Method for synthesizing cubic boron nitride | |
| US4045186A (en) | Method for producing large soft hexagonal boron nitride particles | |
| US3920798A (en) | Zeolite y synthesis | |
| JP3257676B2 (en) | How to grow crystals | |
| JPH02293318A (en) | Production of magnesite, its use for produc- tion of magnesium fluoride and magnesium fluoride obtained by this method | |
| US2131374A (en) | Dolomitic magnesium carbonate composition and method of preparation | |
| US2773738A (en) | New crystalline sodium borate and method for producing the same | |
| JPH0254318B2 (en) | ||
| US3468801A (en) | Synthesis of garnet at high pressures | |
| JP3340319B2 (en) | Method for producing fibrous magnesium borate hydroxide and fibrous magnesium pyroborate | |
| JPS6225601B2 (en) | ||
| JPS6253218B2 (en) | ||
| JPS5869799A (en) | Manufacturing method of fibrous potassium titanate | |
| JPH1192137A (en) | Production of aluminum fluoride particles | |
| CN111893568A (en) | A kind of preparation method of high-purity NaAlB14 crystal | |
| RU2034642C1 (en) | Charge for producing monocrystals of cubical boron nitride | |
| JPS6225602B2 (en) | ||
| JPS5938164B2 (en) | Manufacturing method of cubic boron nitride | |
| JPH052613Y2 (en) | ||
| JPH0691955B2 (en) | Method for synthesizing high quality cubic boron nitride single crystal | |
| JPH0342933B2 (en) |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |