JP2010235369A - Method of synthesizing cubic boron nitride and method of manufacturing cubic boron nitride sintered compact - Google Patents
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- 230000002194 synthesizing effect Effects 0.000 title claims abstract description 19
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 18
- 229910052582 BN Inorganic materials 0.000 title claims description 26
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 title claims description 26
- 238000000034 method Methods 0.000 title claims description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 81
- 229910052751 metal Inorganic materials 0.000 claims abstract description 79
- 239000002184 metal Substances 0.000 claims abstract description 79
- 239000000843 powder Substances 0.000 claims abstract description 42
- 238000005245 sintering Methods 0.000 claims abstract description 37
- 239000002994 raw material Substances 0.000 claims abstract description 28
- 239000011812 mixed powder Substances 0.000 claims abstract description 26
- 239000000956 alloy Substances 0.000 claims abstract description 18
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 18
- 229910052742 iron Inorganic materials 0.000 claims abstract description 17
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 10
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 10
- 239000000203 mixture Substances 0.000 claims description 46
- 229910052804 chromium Inorganic materials 0.000 abstract description 10
- 239000003863 metallic catalyst Substances 0.000 abstract 1
- 238000010189 synthetic method Methods 0.000 abstract 1
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- 239000011777 magnesium Substances 0.000 description 16
- 230000009471 action Effects 0.000 description 11
- 239000007791 liquid phase Substances 0.000 description 11
- 230000001737 promoting effect Effects 0.000 description 10
- 229910052750 molybdenum Inorganic materials 0.000 description 9
- 230000006911 nucleation Effects 0.000 description 9
- 238000010899 nucleation Methods 0.000 description 9
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- 238000002441 X-ray diffraction Methods 0.000 description 7
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- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 229910052796 boron Inorganic materials 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
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- 238000002844 melting Methods 0.000 description 6
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- 238000001308 synthesis method Methods 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 230000035484 reaction time Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910052723 transition metal Inorganic materials 0.000 description 4
- 150000003624 transition metals Chemical class 0.000 description 4
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 3
- 229910020639 Co-Al Inorganic materials 0.000 description 3
- 229910020675 Co—Al Inorganic materials 0.000 description 3
- 229910000943 NiAl Inorganic materials 0.000 description 3
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000011780 sodium chloride Substances 0.000 description 3
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- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- 229910002515 CoAl Inorganic materials 0.000 description 1
- -1 Fe and Co Chemical class 0.000 description 1
- 229910000997 High-speed steel Inorganic materials 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 1
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- PMHQVHHXPFUNSP-UHFFFAOYSA-M copper(1+);methylsulfanylmethane;bromide Chemical compound Br[Cu].CSC PMHQVHHXPFUNSP-UHFFFAOYSA-M 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
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Abstract
Description
本発明は、六方晶窒化ホウ素（以下、ｈＢＮで示す）から立方晶窒化ホウ素（以下、ｃＢＮで示す）を合成するｃＢＮの合成方法であって、かつ、合成したｃＢＮを原料粉末とするｃＢＮ焼結体の製造方法に関する。 The present invention relates to a cBN synthesis method for synthesizing cubic boron nitride (hereinafter referred to as cBN) from hexagonal boron nitride (hereinafter referred to as hBN), and a cBN sintering process using the synthesized cBN as a raw material powder. The present invention relates to a method for producing a bonded body.
従来、ｈＢＮからｃＢＮを合成する合成方法としては、アルカリあるいはアルカリ土類元素を含むホウチッ化物（代表的な例はＬｉ３ＢＮ２）を触媒として用いる方法が一般的なものとして知られているが、Ｃｏ，Ｎｉ，Ｆｅなどの遷移金属とＡｌの合金、混合物も有効な触媒であることも知られている。 Conventionally, as a synthesis method for synthesizing cBN from hBN, a method using a boride containing an alkali or alkaline earth element (typically Li 3 BN 2 ) as a catalyst is generally known. It is also known that alloys of Al, transition metals such as Co, Ni and Fe, and mixtures thereof are effective catalysts.
例えば、特許文献１には、ＮｉＡｌ、ＣｏＡｌ、ＦｅＮｉＡｌ、ＦｅＮｉＣｏＡｌなどの各合金が、圧力およそ６〜８．５ＧＰａ、温度８００〜１６００℃の条件で触媒作用を有することが報告されている。
For example,
特許文献２には、Ｆｅ４６−Ｎｉ３２−Ｃｒ２１−Ａｌ１ｗｔ％、Ｎｉ３９．２−Ｍｎ５８．８−Ａｌ２ｗｔ％、Ｎｉ４９−Ｃｒ４９−Ａｌ２ｗｔ％、Ｆｅ８−Ｎｉ４３−Ｃｒ４７−Ａｌ２ｗｔ％などの混合物が、圧力５〜５．５ＧＰａ、温度約１４００〜１５００℃の範囲で、原料ｈＢＮをｃＢＮに転換する触媒として効果があることが報告されている。
In
非特許文献１には、あらかじめアーク溶解炉で合金化したＦｅ９０−Ａｌ１０ｗｔ％の組成の合金が、約６ＧＰａ以上でｃＢＮ合成触媒として有効であると報告されている。
Non-Patent
また、触媒を用いてｈＢＮからｃＢＮを合成した後、これを焼結することによって、ｃＢＮ焼結体を製造し得ることも知られている。
例えば、特許文献３には、Ｃｏ−Ａｌ混合物、Ｎｉ８７−Ａｌ１３ｗｔ％混合物、ＷＣ−Ｃｏ−Ａｌ、ＮｉＡｌ３合金、Ｃｏ６７−Ｗ１６．５−Ａｌ１６．５ｗｔ％などを原料ｈＢＮと共存させ、圧力５．４ＧＰａ以上、温度範囲は約１５００〜１５５０℃で合成することによってｃＢＮを生成させると、合成されたｃＢＮは構成粒子が強固に結合した焼結体となることが報告されている。
It is also known that a cBN sintered body can be produced by synthesizing cBN from hBN using a catalyst and then sintering it.
For example, in
ｃＢＮは、ダイヤモンドに匹敵する硬度を持つほか、熱的、化学的にも安定であることから、ｃＢＮ焼結体は、例えば、高速度鋼、ダイス鋼、鋳鉄等の鉄系被削材の切削工具用硬質材料等として幅広い分野で利用されている。
ところで、ｈＢＮからｃＢＮを合成する際には、前記従来技術にも示したように、通常超高圧（５ＧＰａ以上）高温条件での合成が行われるが、ｃＢＮ材料の大型化、生産性の向上等を目的として、特に、合成装置の大型化を図ったような場合には、（５ＧＰａ以上の）超高圧が必要であるか否かによって、操業の難易度、装置構成に大きな違いがあり、また、例えば、金型装置の中心部材である大型超硬合金の寿命も操業圧力が超高圧（５ＧＰａ以上）であるか否かによって格段の違いが生じる。
したがって、合成装置を大型化し、生産性の向上を図ったような場合にも、より緩和された低圧条件下で簡易にｃＢＮを合成することができるｃＢＮの合成方法が望まれている。
一方、ｃＢＮ焼結体についても、より緻密で高硬度のｃＢＮ焼結体を製造する方法が望まれている。
Since cBN has hardness comparable to diamond and is also thermally and chemically stable, cBN sintered bodies are used for cutting high-speed steel, die steel, cast iron and other iron-based work materials. It is used in a wide range of fields as a hard material for tools.
By the way, when synthesizing cBN from hBN, as shown in the prior art, synthesis is usually performed under ultra-high pressure (5 GPa or more) and high temperature conditions. In particular, when the size of the synthesizer is increased, there are significant differences in the operational difficulty and device configuration depending on whether or not an ultra-high pressure (over 5 GPa) is required. For example, the life of a large cemented carbide, which is the central member of a mold apparatus, varies greatly depending on whether or not the operating pressure is extremely high (5 GPa or more).
Therefore, there is a demand for a method for synthesizing cBN capable of easily synthesizing cBN under more relaxed low-pressure conditions even when the synthesis apparatus is enlarged and productivity is improved.
On the other hand, a method for producing a denser and harder cBN sintered body is desired for the cBN sintered body.
本発明者らは、ｈＢＮからｃＢＮを合成するに当たって、従来よりも低圧力条件（最低合成圧力が４ＧＰａ）で合成する方法について鋭意研究した結果、次のような知見を得た。 As a result of intensive studies on a method for synthesizing cBN from hBN under a lower pressure condition (minimum synthesis pressure is 4 GPa), the inventors have obtained the following knowledge.
ｈＢＮからｃＢＮを合成するに当たって、従来は、Ｆｅ，Ｎｉ，Ｃｏなどの遷移金属とＡｌとの合金、混合物からなる金属触媒を用いていたが、その反応メカニズムは、まず、超高圧高温条件下で金属触媒が溶融して液相状態になり、該液相中にｈＢＮの成分Ｂ（ホウ素）とＮ（窒素）が溶解し、その後ｃＢＮの核発生・成長が生じ、ｃＢＮの合成が進行すると考えられることから、Ｂ及びＮの上記液相への溶解度が小さいような場合には、ｃＢＮが生成するに必要な条件が満足されず、また、仮に、上記液相中に十分なＢとＮが溶解したとしても、ｃＢＮの熱力学的平衡条件付近（例えば、従来の合成圧力よりも低い４〜５ＧＰａという圧力条件）でｃＢＮの核発生・成長を行わせｃＢＮを合成するためには、ｃＢＮの核発生・成長を促進・助長する条件が必要となると考えられる。
したがって、金属触媒が液相状態でＢ溶解能力及びＮ溶解能力に優れ、同時に、ｃＢＮの核生成・成長を促進・助長する作用を有する場合には、従来よりも低圧力条件下でｈＢＮからｃＢＮを合成することができるといえる。
In the synthesis of cBN from hBN, conventionally, a metal catalyst comprising an alloy or mixture of transition metals such as Fe, Ni, Co and Al was used, but the reaction mechanism was first under ultra high pressure and high temperature conditions. It is thought that the metal catalyst melts into a liquid phase and the components B (boron) and N (nitrogen) of hBN dissolve in the liquid phase, and then nucleation and growth of cBN occurs and the synthesis of cBN proceeds. Therefore, in the case where the solubility of B and N in the liquid phase is small, the conditions necessary for forming cBN are not satisfied, and if sufficient B and N are present in the liquid phase, Even if dissolved, in order to synthesize cBN by nucleating and growing cBN near the thermodynamic equilibrium condition of cBN (for example, 4-5 GPa lower than the conventional synthesis pressure) Promote nucleation and growth It is considered a condition for promoting is required.
Therefore, when the metal catalyst has an excellent B-dissolving ability and N-dissolving ability in a liquid phase state, and at the same time has an action of promoting and promoting nucleation / growth of cBN, it is possible to convert cBN to cBN under a lower pressure condition than before. It can be said that can be synthesized.
ところで、従来用いられてきた金属触媒について、上記の観点から触媒成分の作用を見ると、Ｆｅ，Ｎｉ，Ｃｏなどの遷移金属は、それらが溶融して液相状態になっているときに数％程度のＢを溶解する能力があり、ホウ素溶解成分の作用を有するが、その一方、Ｎを溶解する能力はきわめて小さいために、特に、低圧条件下で合成を行おうとした場合には、結果として、ｃＢＮへの転換反応が極めて不満足なものとなる。 By the way, regarding the conventionally used metal catalysts, when the action of the catalyst component is seen from the above viewpoint, transition metals such as Fe, Ni, Co and the like are several percent when they are melted and in a liquid phase state. It has the ability to dissolve a certain amount of B, and has the effect of a boron-dissolving component, while the ability to dissolve N is extremely small. , The conversion reaction to cBN becomes extremely unsatisfactory.
そこで、本発明者等は、Ｎ溶解能力に優れ、同時に、低圧条件下でもｃＢＮの核生成・成長を促進・助長する作用を有する金属触媒について研究を進めたところ、金属触媒の成分としてＣｒを含有させると、液相状態において、ＣｒがＮを溶解する能力が大であり、また、同じく金属触媒の成分としてＡｌ及びＭｇのいずれか１種又は両者を含有させると、ｃＢＮの核発生・成長が促進・助長され、４〜５ＧＰａという従来の合成圧力よりも低い圧力条件においてもｃＢＮが合成されることを見出した。 Therefore, the present inventors conducted research on a metal catalyst that has an excellent ability to dissolve N and at the same time promotes / promotes cBN nucleation / growth even under low pressure conditions. As a result, Cr was used as a component of the metal catalyst. When contained, Cr has a large ability to dissolve N in the liquid phase state. Similarly, when one or both of Al and Mg are contained as a component of the metal catalyst, nucleation / growth of cBN It was found that cBN was synthesized even under pressure conditions lower than the conventional synthesis pressure of 4-5 GPa.
また、遷移金属のうちのＮｉは、Ｆｅ，Ｃｏと同様に、ホウ素溶解成分の作用を有するものの、その反面、ｃＢＮの合成最低圧力を高くする傾向を有することから、金属触媒の成分としてＮｉを用いる場合には、その含有割合は少量に留めることが必要であることを見出した。
また、ＣｒとＭｏが共存する場合、Ｃｒ単独よりも生成するｃＢＮ粒子径が増大する。これは、Ｃｒに対して、Ｍｏ添加によってチッ素の溶解度が増加するためと考えられる。
Ni in the transition metal, like Fe and Co, has the action of a boron-dissolving component, but on the other hand, it tends to increase the minimum synthesis pressure of cBN, so Ni is used as a component of the metal catalyst. When using, it discovered that the content rate needed to be kept small.
Moreover, when Cr and Mo coexist, the cBN particle diameter produced | generated increases rather than Cr alone. This is presumably because the solubility of nitrogen increases with the addition of Mo to Cr.
つまり、ｈＢＮからｃＢＮを合成する際の金属触媒として、Ｎを溶解する作用を有するＣｒ単独、あるいは、ＣｒとＭｏの両者と、ｃＢＮ核発生・成長を促進・助長する作用を有するＡｌ、Ｍｇ成分と、残部はＢを溶解する作用を有するＦｅ，Ｃｏ成分（及び更に少量のＮｉ成分）からなる合金粉末あるいは混合粉末を用いることによって、合成最低圧力を４ＧＰａにまで低下させることができ、その結果、従来よりも低圧力範囲でｃＢＮを合成できることを見出したのである。 That is, as a metal catalyst for synthesizing cBN from hBN, Cr alone having the action of dissolving N, or both Cr and Mo, and Al and Mg components having the action of promoting and promoting the generation and growth of cBN nuclei The balance can be reduced to 4 GPa by using an alloy powder or mixed powder composed of Fe and Co components (and a small amount of Ni component) having an action of dissolving B, and as a result. The inventors have found that cBN can be synthesized in a lower pressure range than before.
さらに、本発明者らは、ｃＢＮを原料粉末とし、上記金属触媒を焼結助剤として用い、原料粉末と焼結助剤との混合粉に対して焼結を行ったところ、ｃＢＮ粒子間で強固な直接結合を有する緻密かつ高硬度のｃＢＮ焼結体が得られることをも見出した。 Furthermore, the present inventors used cBN as a raw material powder, the above metal catalyst as a sintering aid, and sintered to a mixed powder of the raw material powder and the sintering aid. It has also been found that a dense and highly hard cBN sintered body having a strong direct bond can be obtained.
本発明は、上記知見に基づいてなされたものであって、
「（１） 金属触媒の存在下、超高圧高温条件で六方晶窒化ホウ素から立方晶窒化ホウ素を合成する立方晶窒化ホウ素の合成方法において、上記金属触媒は、１５ｗｔ％以上５５ｗｔ％以下のＣｒと、１．５〜８ｗｔ％のＡｌ及びＭｇのいずれか１種又は２種と、残部はＦｅ及びＣｏのいずれか１種又は２種の成分組成からなる合金粉末あるいは混合粉末であって、さらに、上記合成を、４ＧＰａ以上、１２００〜１９００℃で行うことを特徴とする立方晶窒化ホウ素の合成方法。
（２） 上記金属触媒が、２２ｗｔ％以下のＮｉを更に含有することを特徴とする前記（１）に記載の立方晶窒化ホウ素の合成方法。
（３） 上記金属触媒が、１５ｗｔ％≦（Ｃｒ＋Ｍｏ）≦５５ｗｔ％を満足するＭｏを更に含有することを特徴とする前記（１）または（２）に記載の立方晶窒化ホウ素の合成方法。
（４） 立方晶窒化ホウ素を原料粉末とし、該原料粉末に焼結助剤を添加して焼結することからなる立方晶窒化ホウ素焼結体の製造方法において、上記焼結助剤として、１５ｗｔ％以上５５ｗｔ％以下のＣｒと、１．５〜８ｗｔ％のＡｌ及びＭｇのいずれか１種又は２種と、残部はＦｅ及びＣｏのいずれか１種又は２種の成分組成からなる合金粉末あるいは混合粉末を、原料粉末に５〜１０体積％添加して焼結することを特徴とする立方晶窒化ホウ素焼結体の製造方法。
（５） 上記焼結助剤が、２２ｗｔ％以下のＮｉを更に含有することを特徴とする前記（４）に記載の立方晶窒化ホウ素焼結体の製造方法。
（６） 上記焼結助剤が、１５ｗｔ％≦（Ｃｒ＋Ｍｏ）≦５５ｗｔ％を満足するＭｏを更に含有することを特徴とする前記（４）または（５）に記載の立方晶窒化ホウ素焼結体の製造方法。」
を特徴とするものである。
The present invention has been made based on the above findings,
“(1) In the method of synthesizing cubic boron nitride in which cubic boron nitride is synthesized from hexagonal boron nitride under ultrahigh pressure and high temperature in the presence of a metal catalyst, the metal catalyst contains 15 wt% or more and 55 wt% or less of Cr. Any one or two of Al and Mg of 1.5 to 8 wt%, and the balance is an alloy powder or mixed powder composed of any one or two of Fe and Co, A method for synthesizing cubic boron nitride, wherein the synthesis is performed at 4 GPa or more and 1200 to 1900 ° C.
(2) The method for synthesizing cubic boron nitride according to (1) above, wherein the metal catalyst further contains 22 wt% or less of Ni.
(3) The method for synthesizing cubic boron nitride according to (1) or (2), wherein the metal catalyst further contains Mo satisfying 15 wt% ≦ (Cr + Mo) ≦ 55 wt%.
(4) In a method for producing a cubic boron nitride sintered body comprising cubic boron nitride as a raw material powder, adding a sintering aid to the raw material powder and sintering, 15 wt. % Or more and 55 wt% or less of Cr, 1.5 to 8 wt% of any one or two of Al and Mg, and the balance is an alloy powder consisting of one or two of Fe and Co. A method for producing a cubic boron nitride sintered body, wherein the mixed powder is added to a raw material powder in an amount of 5 to 10% by volume and sintered.
(5) The method for producing a cubic boron nitride sintered body according to (4), wherein the sintering aid further contains 22 wt% or less of Ni.
(6) The cubic boron nitride sintered body according to (4) or (5), wherein the sintering aid further contains Mo satisfying 15 wt% ≦ (Cr + Mo) ≦ 55 wt%. Manufacturing method. "
It is characterized by.
本発明について、以下に詳細に説明する。 The present invention will be described in detail below.
金属触媒の成分・組成：
請求項１記載の発明では、金属触媒は、１５ｗｔ％以上５５ｗｔ％以下のＣｒと、１．５〜８ｗｔ％のＡｌ及びＭｇのいずれか１種又は２種と、残部はＦｅ及びＣｏのいずれか１種又は２種からなる合金粉末あるいは混合粉末として形成される。
Ｃｒ成分は、原材料であるｈＢＮのＮを溶融状態（液相）の金属触媒に溶解する作用を有するが、Ｃｒ成分の含有割合が１５ｗｔ％未満では、Ｎの溶解量が少ないためｃＢＮが十分生成されず、一方、Ｃｒ成分の含有割合が５５ｗｔ％を超えると、金属触媒の溶融温度が高くなりすぎるために４〜５ＧＰａという低圧力条件ではＮの溶解度が低下しｃＢＮが十分生成されないため、Ｎを溶解する作用を有するＣｒ成分の含有割合は１５ｗｔ％以上５５ｗｔ％以下、好ましくは、２０〜４０ｗｔ％、と定めた。
Ａｌ成分、Ｍｇ成分は、いずれも、ｃＢＮの核発生・成長を促進・助長する作用を有し、金属触媒に少量添加含有させることで、ｃＢＮ合成時の必要圧力を大きく低下させ、４〜５ＧＰａの低圧条件でのｃＢＮの合成を可能とするが、Ａｌ成分、Ｍｇ成分あるいは両者の合計含有割合が１．５ｗｔ％未満では、ｃＢＮの核発生・成長の促進・助長作用が少ないためｃＢＮの形成が不十分となり、一方、Ａｌ成分が多すぎると窒化アルミニウムが生成してｃＢＮ生成の阻害要因となることがあり、また、Ｍｇ成分が多すぎるとホウ窒化マグネシウムが生成する可能性があり、焼結体を形成する上で望ましくないので、Ａｌ成分及びＭｇ成分のいずれか１種又は２種の含有割合（但し、Ａｌ成分とＭｇ成分の合計含有割合）を、１．５〜８ｗｔ％と定めた。
Ｆｅ及びＣｏのいずれか１種又は２種の成分は、夫々単独でも、また、これらを２種を組み合わせた場合でも、原材料であるｈＢＮのＢを、溶融状態（液相）の金属触媒に溶解する作用を有する。
なお、本発明の金属触媒は、所定の組成となるように各成分を混合した後、予めアーク溶解法、アトマイズ法等で合金化した合金粉末の形態で使用できるほか、各成分の粉末を所定の組成（配合）となるように配合しこれを混合した混合粉末の形態で使用することができる。
Components and composition of metal catalyst:
In the first aspect of the present invention, the metal catalyst is 15 wt% or more and 55 wt% or less of Cr, 1.5 to 8 wt% of any one or two of Al and Mg, and the balance is either Fe or Co. It is formed as an alloy powder or mixed powder composed of one or two kinds.
The Cr component has the effect of dissolving N of hBN, which is a raw material, in a metal catalyst in a molten state (liquid phase). However, if the Cr component content is less than 15 wt%, the amount of dissolved N is small, so that sufficient cBN is generated. On the other hand, if the content ratio of the Cr component exceeds 55 wt%, the melting temperature of the metal catalyst becomes too high, so that the solubility of N is reduced under low pressure conditions of 4 to 5 GPa and cBN is not sufficiently generated. The content ratio of the Cr component having an action of dissolving the selenium was 15 wt% or more and 55 wt% or less, preferably 20 to 40 wt%.
Both the Al component and the Mg component have the effect of promoting and promoting cBN nucleation / growth, and by adding a small amount to the metal catalyst, the required pressure at the time of cBN synthesis is greatly reduced to 4-5 GPa. CBN can be synthesized under low pressure conditions, but if the total content of the Al component, the Mg component, or both is less than 1.5 wt%, cBN nucleation, growth promotion, and promoting effect are small, and cBN formation On the other hand, if there is too much Al component, aluminum nitride may be generated and hinder the generation of cBN, and if there is too much Mg component, magnesium boronitride may be generated. Since it is not desirable for forming a bonded body, the content ratio of one or two of the Al component and the Mg component (however, the total content ratio of the Al component and the Mg component) is 1.5 to 8 wt%. It determined.
Either one or two components of Fe and Co can be used alone or in combination of two of them, and B of raw material hBN can be dissolved in a molten (liquid phase) metal catalyst. Has the effect of
The metal catalyst of the present invention can be used in the form of an alloy powder that is previously alloyed by an arc melting method, an atomizing method, etc. after mixing each component so as to have a predetermined composition. It can be used in the form of a mixed powder obtained by mixing and mixing so as to have the composition (mixing).
請求項２、３記載の発明では、金属触媒は、２２ｗｔ％以下のＮｉを更に含有し、あるいは、１５ｗｔ％≦（Ｃｒ＋Ｍｏ）≦５５ｗｔ％を満足するＭｏを更に含有する。
Ｎｉ成分は、Ｆｅ、Ｃｏと同様に、ｈＢＮのＢを、溶融状態（液相）の金属触媒に溶解する作用を有するが、その反面、Ｎｉ成分の含有割合が、２２ｗｔ％を超えると、ｃＢＮ合成に際しての合成最低圧力を５Ｇａ以上に高くすることから、より低圧条件下でｃＢＮを合成するという本発明の観点からは、金属触媒の成分としてＮｉを用いる場合のＮｉ成分の含有割合は２２ｗｔ％以下に制限することが必要である。
また、Ｍｏ成分はＣｒ成分と同様、溶融状態の金属の成分として存在している場合、それぞれ、Ｎの溶解度を向上させる。単独でも効果があるが、適当なＣｒとＭｏの組成比を選択すると、相乗的にＮの溶解度が向上する。
ただし、Ｃｒ＋Ｍｏ添加において、Ｃｒ成分とＭｏ成分の合計含有割合が１５ｗｔ％未満となる場合には、ｃＢＮの合成に際し、金属触媒の成分として、Ｃｒ、Ｍｏを含有させたことによる溶融状態（液相）の金属触媒にＮを溶解する作用が低減し、低圧条件でｃＢＮの合成を行うことが困難となり、一方、Ｃｒ成分とＭｏ成分の合計含有割合が５５ｗｔ％を超えると、必然的に、ホウ素溶解成分であるＦｅ，Ｃｏ，Ｎｉなどの組成比が減少するから、融点上昇やホウ素の溶解度の低下によって、ｃＢＮの合成圧力が上昇する。また、ｃＢＮ焼結体を製造する場合、ｃＢＮ粒子間に存在せしめる金属の融点が上昇して好ましくない。
それ故、Ｃｒ成分とＭｏ成分の合計含有割合は、１５ｗｔ％以上５５ｗｔ％以下を満足することが必要である。
In the second and third aspects of the invention, the metal catalyst further contains 22 wt% or less of Ni, or further contains Mo satisfying 15 wt% ≦ (Cr + Mo) ≦ 55 wt%.
The Ni component has an action of dissolving B of hBN in a molten (liquid phase) metal catalyst, similarly to Fe and Co. On the other hand, when the content ratio of the Ni component exceeds 22 wt%, cBN From the viewpoint of the present invention of synthesizing cBN under a lower pressure condition since the minimum synthesis pressure at the time of synthesis is increased to 5 Ga or more, the content ratio of the Ni component when using Ni as the metal catalyst component is 22 wt%. It is necessary to limit to:
Further, like the Cr component, the Mo component improves the solubility of N when present as a molten metal component. Although it is effective by itself, the solubility of N is synergistically improved when an appropriate composition ratio of Cr and Mo is selected.
However, in the case of adding Cr + Mo, when the total content ratio of the Cr component and the Mo component is less than 15 wt%, in the synthesis of cBN, the molten state (liquid phase) by containing Cr and Mo as components of the metal catalyst ), The effect of dissolving N in the metal catalyst is reduced, and it is difficult to synthesize cBN under low pressure conditions. On the other hand, if the total content of Cr component and Mo component exceeds 55 wt%, boron is inevitably produced. Since the composition ratio of Fe, Co, Ni, etc., which are dissolved components, decreases, the synthesis pressure of cBN increases due to an increase in melting point and a decrease in boron solubility. Moreover, when manufacturing a cBN sintered compact, the melting | fusing point of the metal which exists between cBN particle | grains raises, and is not preferable.
Therefore, the total content ratio of the Cr component and the Mo component needs to satisfy 15 wt% or more and 55 wt% or less.
合成条件（圧力、温度）：
ｈＢＮからｃＢＮへの合成は、例えば、図１に示す合成装置内に、合成用原材料であるｈＢＮと上記金属触媒の粉末を共存させた状態で配置し、圧力４ＧＰａ以上、温度１２００〜１９００℃で合成することによって行うことができる。
この発明では、上記金属触媒を用いることにより、ｃＢＮの最低合成圧力を４ＧＰａにまで低減することができ、従来の合成法に比し、はるかに低圧力範囲（好ましくは、４．４ＧＰａ以上）でｃＢＮの合成を行うことができる（勿論、従来法における合成圧力、例えば、５〜８．５ＧＰａという高圧で合成を行うことも可能であるが）ため、設備の大型化が不要になり、装置構成部材の耐用寿命も延びる等のメリットがある。
合成温度が１２００℃未満では、金属触媒の溶解が生じないためｃＢＮの合成反応が進行せず、一方、１９００℃を超えると、ｈＢＮ⇔ｃＢＮの圧力・温度平衡状態により４〜５ＧＰａ圧力領域においては１９００℃以上がｈＢＮの安定領域のため、合成したｃＢＮがｈＢＮに逆変換する恐れがあることから、反応合成温度を１２００〜１９００℃（好ましくは、１３００〜１７５０℃）と定めた。
Synthesis conditions (pressure, temperature):
In the synthesis from hBN to cBN, for example, in the synthesis apparatus shown in FIG. 1, hBN, which is a raw material for synthesis, and the above metal catalyst powder are coexisted, and the pressure is 4 GPa or more and the temperature is 1200 to 1900 ° C. This can be done by synthesis.
In this invention, by using the above metal catalyst, the minimum synthesis pressure of cBN can be reduced to 4 GPa, and in a much lower pressure range (preferably 4.4 GPa or more) compared to the conventional synthesis method. Since it is possible to synthesize cBN (of course, it is possible to synthesize at a synthesis pressure in the conventional method, for example, a high pressure of 5 to 8.5 GPa), it is not necessary to increase the size of the equipment, and the device configuration There are advantages such as extending the useful life of the member.
When the synthesis temperature is less than 1200 ° C., the metal catalyst does not dissolve, so the synthesis reaction of cBN does not proceed. On the other hand, when the synthesis temperature exceeds 1900 ° C., in the pressure range of 4-5 GPa due to the pressure / temperature equilibrium state of hBN⇔cBN. Since 1900 ° C. or higher is a stable region of hBN, the synthesized cBN may be converted back to hBN. Therefore, the reaction synthesis temperature was set to 1200 to 1900 ° C. (preferably 1300 to 1750 ° C.).
ｃＢＮ焼結体：
従来、例えば、特許文献３に記載されたように、ＷＣ−Ｃｏ−Ａｌ、ＮｉＡｌ３、Ｃｏ６７−Ｗ１６．５−Ａｌ１６．５ｗｔ％などを焼結助剤とし、ｃＢＮ粒子が強固に結合した焼結体を作製するためには、圧力５．４ＧＰａ以上、温度１５００℃以上で行わなければならなかったが、本発明によれば、ｃＢＮを原料粉末とし、ｃＢＮの合成に用いた前記特定の成分組成の合金粉末あるいは混合粉末からなる金属触媒を焼結助剤として用い、焼結助剤の配合割合が５〜１０体積％となるように原料粉末に配合し、例えば、図２に示す焼結装置内にこの混合粉末を配置し、例えば、４．０〜６．０ＧＰａで加圧しながら、１２００〜２０００℃の温度範囲で焼結すると、ｃＢＮ粒子間に強固な直接結合を有する緻密かつ高硬度のｃＢＮ焼結体を得ることができる。つまり、ｃＢＮ合成時に用いる上記金属触媒は、ｃＢＮ焼結体を製造する際の焼結助剤としての機能も備えるといえる。
例えば、図１に示す合成装置により、本発明の合成法で合成（金属触媒としては、Ｃｏ５８．２−Ｃｒ３８．８−Ａｌ３ｗｔ％の成分組成のＣｏ−Ｃｒ−Ａｌ系の金属触媒を使用）したｃＢＮ粉末を原料粉末とし、上記金属触媒と同一成分組成のＣｏ−Ｃｒ−Ａｌ系合金を焼結助剤として用い、焼結助剤の含有割合が、１０体積％となるように配合し、これを図２に示す焼結装置で、４．７ＧＰａ×１４８０〜１４９０℃の条件で焼結することによってｃＢＮ焼結体を製造した。本発明により得られたｃＢＮ焼結体の走査型電子顕微鏡写真による組織の一例を図４に示す。
すなわち、本発明の製造法で得られたｃＢＮ焼結体は、低温度での焼結であっても、非常に緻密な組織を有すると同時に、極めて高い硬度を有することが分かる。
たとえば、本発明例８においては、低温度（１６００℃）の焼結であるにもかかわらず、緻密な組織を有する（図４参照）と同時に、Ｈｖ：３４００という極めて高い硬度が得られている。
cBN sintered body:
Conventionally, for example, as described in
For example, the synthesis was performed by the synthesis method of the present invention using the synthesis apparatus shown in FIG. 1 (as the metal catalyst, a Co—Cr—Al-based metal catalyst having a component composition of Co 58.2-Cr 38.8-
That is, it can be seen that the cBN sintered body obtained by the production method of the present invention has a very dense structure and at the same time has an extremely high hardness even when sintered at a low temperature.
For example, in Example 8 of the present invention, despite having a low temperature (1600 ° C.) sintering, it has a dense structure (see FIG. 4) and at the same time has an extremely high hardness of Hv: 3400. .
上記のとおり、本発明は、特定の成分組成の金属触媒を用いてｈＢＮからｃＢＮを合成することにより、最低合成圧力を低下させることができるため従来に比し低圧力範囲（４ＧＰａ以上）で合成を行うことができ、ｃＢＮ合成装置の大型化を必要とせず、設備費の低減を図ることができ、さらに、ｃＢＮ合成装置構造部材の長寿命化を図ることができる。
また、ｃＢＮを原料粉末とし、上記金属触媒と同一成分組成の合金粉末、混合粉末を焼結助剤として用いて焼結を行うと、他の焼結所剤を用いることなしに、ｃＢＮ粒子間に強固な直接結合を有すると同時に、緻密な組織な組織を有し、かつ、高硬度のｃＢＮ焼結体を製造することができ、ｃＢＮ焼結体製造の低コスト化を図ることもできる。
As described above, the present invention can synthesize cBN from hBN using a metal catalyst having a specific component composition, so that the lowest synthesis pressure can be reduced. Therefore, the synthesis is performed in a lower pressure range (4 GPa or more) than in the past. Therefore, it is not necessary to increase the size of the cBN synthesizer, the equipment cost can be reduced, and the life of the structural member of the cBN synthesizer can be extended.
In addition, when cBN is used as a raw material powder and sintering is performed using an alloy powder having the same composition as the metal catalyst and a mixed powder as a sintering aid, the inter-cBN particles can be formed without using other sintering agents. It is possible to produce a cBN sintered body having a dense structure and a dense structure and a high hardness, and to reduce the cost of producing the cBN sintered body.
以下に、本発明のｃＢＮ合成方法、ｃＢＮ焼結体の製造方法について、実施例に基づいて具体的に説明する。 Hereinafter, the cBN synthesis method and the cBN sintered body manufacturing method of the present invention will be specifically described based on examples.
本発明例１：
図１に示すように、金属触媒として、Ｃｏ５８．２−Ｃｒ３８．８−Ａｌ３ｗｔ％からなる成分組成の合金粉末をあらかじめ作り、約７ｍｍ径で３ｍｍ厚さの２枚のｈＢＮ成形板（４）間に約１．６ｍｍ厚さのサンドイッチされた金属触媒（合金粉末）層（３）が形成されるように、外径１０ｍｍ，内径７ｍｍ，高さ７．６ｍｍの食塩（ジルコニア粉末を１０ｗｔ％含む）成形体（５）の試料容器中に充填した。
これらの試料を、外径１２ｍｍ，内径１０ｍｍ，高さ１７．６ｍｍのグラファイト管状ヒーター（１）で囲み、内面にはＭｏ箔（２）を配置し、ベルト型超高圧装置（アンビル先端径２１ｍｍ，シリンダー内径２５ｍｍ）で加圧し、その後ヒーターに電力を投入して加熱して、一定時間保持後、急速に温度を下げ、その後除圧して試料を取り出し、光学顕微鏡、Ｘ線回折などの手法で試料を同定した。
圧力４．７ＧＰａ、１４３６℃で１時間反応させた試料を解析した結果、全体が黄色の０．２ｍｍ程度のｃＢＮ粒子と金属相との混合物であり、ｃＢＮの合成が起こったことがわかった。
また、上記と同じ成分組成の混合粉末を金属触媒として、圧力４．２ＧＰａ、１３７０℃で１時間反応させたところ、約１．５ｍｍの原料層が、ｃＢＮ粒子と金属相との混合物に転換し、やはりｃＢＮの合成が行われたことがわかる。
ここで、Ｘ線回折は、ブルカー製ＡＸＳＭＸＰ１８ＶＡＨＦにより測定を行った。
Invention Example 1:
As shown in FIG. 1, an alloy powder having a composition of Co58.2-Cr38.8-Al3 wt% is prepared in advance as a metal catalyst, and is formed between two hBN molded plates (4) having a diameter of about 7 mm and a thickness of 3 mm. So that a sandwiched metal catalyst (alloy powder) layer (3) having a thickness of about 1.6 mm is formed on the outer surface of sodium chloride (including 10 wt% of zirconia powder) having an outer diameter of 10 mm, an inner diameter of 7 mm, and a height of 7.6 mm. It filled in the sample container of the molded object (5).
These samples were surrounded by a graphite tubular heater (1) having an outer diameter of 12 mm, an inner diameter of 10 mm, and a height of 17.6 mm, Mo foil (2) was disposed on the inner surface, and a belt type ultrahigh pressure apparatus (anvil tip diameter of 21 mm, Pressurize with a cylinder inner diameter of 25 mm), and then apply power to the heater to heat it, hold it for a certain period of time, then rapidly lower the temperature, then remove the pressure and take out the sample, and use a method such as optical microscopy or X-ray diffraction Was identified.
As a result of analyzing the sample reacted for 1 hour at a pressure of 4.7 GPa and 1436 ° C., it was found that the whole was a mixture of yellow cBN particles of about 0.2 mm and a metal phase, and cBN synthesis occurred.
Moreover, when a mixed powder having the same composition as described above was used as a metal catalyst and reacted at a pressure of 4.2 GPa and 1370 ° C. for 1 hour, the raw material layer of about 1.5 mm was converted into a mixture of cBN particles and a metal phase. It can also be seen that cBN was synthesized.
Here, X-ray diffraction was measured by Bruker AXSMXP18VAHF.
本発明例２：
２〜４μｍの粒度のｃＢＮを原料粉末とし、焼結助剤として、上記金属触媒と同一成分組成からなる混合粉末（Ｃｏ５８．２−Ｃｒ３８．８−Ａｌ３ｗｔ％）を用い、焼結助剤の含有割合が１０体積％となるよう配合した混合粉末（２）を、図２に示すように０．０２ｍｍ厚さのＭｏ箔で内側を囲んだ外径１０ｍｍ、内径７ｍｍ、高さ７．６ｍｍの食塩（ジルコニア粉末を１０ｗｔ％含む）成形体（５）間にサンドイッチされるように充填し、圧力４．７ＧＰａ、１４８０〜１４９０℃で０．５時間焼結した。
得られたｃＢＮ焼結体を走査型電子顕微鏡で観察したところ、各ｃＢＮ粒子間に強固な直接結合を有し、緻密な焼結組織を有するとともに、得られたｃＢＮ焼結体は、高硬度を有していた。
Invention Example 2:
CBN having a particle size of 2 to 4 μm is used as a raw material powder, and a mixed powder (Co58.2-Cr38.8-Al3 wt%) having the same composition as the metal catalyst is used as a sintering aid, The mixed powder (2) blended so as to have a ratio of 10% by volume is salted with an outer diameter of 10 mm, an inner diameter of 7 mm, and a height of 7.6 mm surrounded by a 0.02 mm-thick Mo foil as shown in FIG. It was filled so as to be sandwiched between shaped bodies (5) (containing 10 wt% of zirconia powder), and sintered at a pressure of 4.7 GPa and 1480 to 1490 ° C. for 0.5 hour.
When the obtained cBN sintered body was observed with a scanning electron microscope, each cBN particle had a strong direct bond, had a dense sintered structure, and the obtained cBN sintered body had a high hardness. Had.
本発明例３：
本発明例１において、Ａｌに替えてＭｇを含有させた金属触媒、即ち、Ｃｏ５８．２−Ｃｒ３８．８−Ｍｇ３ｗｔ％組成の金属触媒、を用いて、圧力４．２ＧＰａ、１３７０℃で１時間反応させたところ、金属触媒層付近に非常に微細なｃＢＮ粒子が析出していたことから、ＭｇはＡｌと同様な作用を有する成分であることがわかる。
Invention Example 3:
In Example 1 of the present invention, a metal catalyst containing Mg instead of Al, that is, a metal catalyst having a composition of Co 58.2-Cr 38.8-
本発明例４：
Ｆｅ５２．３８−Ｃｒ３８．８−Ｎｉ５．８２−Ａｌ３ｗｔ％からなる成分組成の混合粉末を金属触媒として用い、本発明例１と同様な方法で、圧力を４．２ＧＰａ、温度は１２８０℃、１３８０℃、１４３５℃の三種類、反応時間１時間で反応させたところ、いずれの場合も、ｃＢＮが合成されていることをＸ線回折により確認した。
Invention Example 4:
Using a mixed powder having a component composition of Fe52.38-Cr38.8-Ni5.82-Al3 wt% as a metal catalyst, the pressure was 4.2 GPa, the temperatures were 1280 ° C. and 1380 ° C. in the same manner as in Example 1 of the present invention. When the reaction was carried out at 1435 ° C. for 3 hours at a reaction time of 1 hour, it was confirmed by X-ray diffraction that cBN was synthesized in all cases.
比較例１：
本発明例４とＦｅ，Ｃｒ，Ｎｉの含有割合が類似するが、Ａｌ成分を全く含有しない成分組成の混合物（Ｆｅ５４−Ｃｒ４０−Ｎｉ６ｗｔ％）を金属触媒として用い、本発明例１と同様な方法で、圧力を５ＧＰａ、温度は１４００℃、反応時間１時間で反応させたところ、金属は溶解していた痕跡は認められるものの、Ｘ線回折によるｃＢＮの存在は全く検出されなかった。
Comparative Example 1:
The same method as in Example 1 of the present invention, using a mixture (Fe54-Cr40-Ni6 wt%) having a composition similar to that of Example 4 of the present invention, but containing no Al component at all, similar in content ratio of Fe, Cr, Ni Then, when the reaction was performed at a pressure of 5 GPa, a temperature of 1400 ° C., and a reaction time of 1 hour, traces of the metal being dissolved were observed, but the presence of cBN was not detected at all by X-ray diffraction.
本発明例３、本発明例４と比較例１の結果から、金属触媒中のＡｌ成分、Ｍｇ成分が、ｃＢＮの低圧合成において、ｃＢＮの核発生・成長を促進・助長する作用を有することがわかる。 From the results of Invention Example 3, Invention Example 4 and Comparative Example 1, it can be seen that the Al component and Mg component in the metal catalyst have the effect of promoting and promoting cBN nucleation / growth in low-pressure synthesis of cBN. Recognize.
本発明例５：
本発明例４と同様に、Ｆｅ５２．３８−Ｃｒ３８．８−Ｎｉ５．８２−Ａｌ３ｗｔ％からなる成分組成の混合粉末を金属触媒として用い、圧力を４．１ＧＰａに変更し、また、温度は１３２５℃、１３４０℃、１３５０℃、１４７０℃の四種類、反応時間１時間で反応させたところ、いずれの場合も、金属皮膜に包まれた約０．３〜０．４ｍｍのｃＢＮ結晶が多量に合成析出していることを確認した。
さらに、上記金属触媒を用い、圧力を４．０ＧＰａに変更し、温度は１３００℃、１３８０℃の二種類、反応時間１時間で反応させたところ、いずれの場合も、金属皮膜に包まれた約０．３〜０．４ｍｍのｃＢＮ結晶がやはり多量に合成析出していた。
Invention Example 5:
Similar to Example 4 of the present invention, a mixed powder having a component composition of Fe 52.38-Cr 38.8-Ni 5.82-
Furthermore, when the metal catalyst was used, the pressure was changed to 4.0 GPa, and the reaction was carried out in two kinds of temperatures, 1300 ° C. and 1380 ° C., with a reaction time of 1 hour. A large amount of 0.3 to 0.4 mm of cBN crystals was also synthesized and precipitated.
本発明例５からもわかるように、本発明の成分組成の金属触媒を使用したときのｃＢＮ最低合成圧力は、４．０ＧＰａであることがわかる。 As can be seen from Example 5 of the present invention, it can be seen that the minimum cBN synthesis pressure when using the metal catalyst having the component composition of the present invention is 4.0 GPa.
本発明例６：
２〜４μｍの粒度のｃＢＮを原料粉末とし、焼結助剤として、Ｆｅ５２．３８−Ｃｒ３８．８−Ｎｉ５．８２−Ａｌ３ｗｔ％の成分組成の混合粉末を用い、焼結助剤の含有割合が１０体積％となるよう配合した混合粉末（２）を、図２に示すように０．０２ｍｍ厚さのＭｏ箔で内側を囲んだ外径１０ｍｍ、内径７ｍｍ、高さ７．６ｍｍの食塩（ジルコニア粉末を１０ｗｔ％含む）成形体（５）間にサンドイッチされるように充填し、圧力４．７ＧＰａ、１４７０℃で０．５時間焼結した。
得られたｃＢＮ焼結体は、各ｃＢＮ粒子間に強固な直接結合を有し、図４に示されると同様な緻密な焼結組織を有しており、かつ、高硬度であった。
Invention Example 6:
CBN having a particle size of 2 to 4 μm is used as a raw material powder, and a mixed powder having a component composition of Fe52.38-Cr38.8-Ni5.82-Al3 wt% is used as a sintering aid, and the content ratio of the sintering aid is 10 As shown in FIG. 2, the mixed powder (2) blended so as to have a volume% is surrounded by 0.02 mm-thick Mo foil, and the outer diameter is 10 mm, the inner diameter is 7 mm, and the height is 7.6 mm. Sodium chloride (zirconia powder) Was packed so as to be sandwiched between the molded bodies (5), and sintered at a pressure of 4.7 GPa and 1470 ° C. for 0.5 hours.
The obtained cBN sintered body had a strong direct bond between the respective cBN particles, had a dense sintered structure similar to that shown in FIG. 4, and had high hardness.
本発明例７：
Ｃｏ４９．２８−Ｃｒ２７．１４−Ｎｉ２０．７１−Ａｌ２．６ｗｔ％からなる成分組成の混合粉末を金属触媒として用い、本発明例１と同様な方法で、４．４ＧＰａ、１４００℃で１時間反応させたところ、全体に多量の微粒子ｃＢＮ結晶が生成していた。
Invention Example 7:
Using a mixed powder having a component composition of Co49.28-Cr27.14-Ni20.71-Al2.6 wt% as a metal catalyst, the mixture was reacted at 4.4 GPa and 1400 ° C. for 1 hour in the same manner as in Example 1 of the present invention. As a result, a large amount of fine particle cBN crystals was formed on the whole.
比較例２，比較例３：
本発明例７の上記金属触媒において、Ｎｉ含有割合を増加させたＣｏ４７．１−Ｃｒ２６．１−Ｎｉ２３．６−Ａｌ２．８ｗｔ％の金属触媒（比較例２）、Ｃｏ４３．８−Ｃｒ２２．３−Ｎｉ２８．８−Ａｌ３．２ｗｔ％の金属触媒（比較例３）を作製し、これを用いて、本発明例１と同様な方法で、５ＧＰａ、１４００℃で１時間反応させたところ、Ｘ線回折によるｃＢＮの存在は全く検出されなかった。
Comparative Example 2 and Comparative Example 3:
Co 47.1-Cr 26.1-Ni 23.6-Al 2.8 wt% metal catalyst (Comparative Example 2), Co 43.8-Cr 22.3- 3 with increased Ni content in the above metal catalyst of Invention Example 7. An Ni28.8-Al3.2 wt% metal catalyst (Comparative Example 3) was prepared and reacted at 5 GPa and 1400 ° C. for 1 hour in the same manner as in Example 1 of the present invention. The presence of cBN due to was not detected at all.
以上のことから、Ｎｉを金属触媒の成分として用いた場合には、Ｎｉ含有割合は、２２ｗｔ％以下としなければならないことがわかる。 From the above, it can be seen that when Ni is used as a component of the metal catalyst, the Ni content must be 22 wt% or less.
本発明例８：
Ｃｏ４６．６−Ｃｒ３１−Ｍｏ２０−Ａｌ２．４ｗｔ％らなる成分組成の混合物を金属触媒として用いて、本発明例１と同様な方法で４．２ＧＰａ，１３００℃で１時間反応させたところ、全体に多量のｃＢＮ粒子が生成した。粒子径は約０．５〜０．９ｍｍの比較的大きなｃＢＮ粒子であった。
ｃＢＮが合成されていることをＸ線回折により確認した。
図３に、得られたｃＢＮのＸ線回折チャート（ｃＢＮピークが存在する）を示す。
さらに、上記により得られたｃＢＮを原料粉末とし、焼結助剤として、上記金属触媒と同一成分組成からなる混合粉末（Ｃｏ４６．６−Ｃｒ３１−Ｍｏ２０−Ａｌ２．４ｗｔ％）を用い、焼結助剤の含有割合が１０体積％となるよう配合した混合粉末（２）を、図２に示すように０．０２ｍｍ厚さのＭｏ箔で内側を囲んだ外径１０ｍｍ、内径７ｍｍ、高さ７．６ｍｍの食塩（ジルコニア粉末を１０ｗｔ％含む）成形体（５）間にサンドイッチされるように充填し、圧力５．５ＧＰａ、１６００℃で１時間焼結した。
得られたｃＢＮ焼結体を走査型電子顕微鏡で観察したところ、各ｃＢＮ粒子間に強固な直接結合を有し、図４に示すように、緻密な焼結組織を有していた。
また、得られたｃＢＮ焼結体は、高硬度（Ｈｖ：３４００）を有していた。
なお、本発明では、ｃＢＮ焼結体の硬さは、ダイヤモンドペーストを研摩剤として焼結体表面を研摩した後、その表面のヴィッカース硬さ（Ｈｖ）を測定することによって求めた。
Invention Example 8:
When a mixture having a component composition of Co46.6-Cr31-Mo20-Al2.4 wt% was used as a metal catalyst, the mixture was reacted at 4.2 GPa and 1300 ° C. for 1 hour in the same manner as in Invention Example 1. A large amount of cBN particles was produced. The particle size was relatively large cBN particles of about 0.5 to 0.9 mm.
It was confirmed by X-ray diffraction that cBN was synthesized.
FIG. 3 shows an X-ray diffraction chart (there is a cBN peak) of the obtained cBN.
Further, the cBN obtained as described above was used as a raw material powder, and a mixed powder (Co46.6-Cr31-Mo20-Al2.4 wt%) having the same composition as that of the metal catalyst was used as a sintering aid. The mixed powder (2) blended so that the content ratio of the agent is 10% by volume is surrounded by a 0.02 mm-thick Mo foil as shown in FIG. 2, and the outer diameter is 10 mm, the inner diameter is 7 mm, and the height is 7. It was filled so as to be sandwiched between 6 mm sodium chloride (containing 10 wt% zirconia powder) compacts (5), and sintered at a pressure of 5.5 GPa and 1600 ° C. for 1 hour.
When the obtained cBN sintered body was observed with a scanning electron microscope, it had a strong direct bond between the cBN particles and had a dense sintered structure as shown in FIG.
Moreover, the obtained cBN sintered body had high hardness (Hv: 3400).
In the present invention, the hardness of the cBN sintered body was obtained by polishing the surface of the sintered body using diamond paste as an abrasive and then measuring the Vickers hardness (Hv) of the surface.
本発明例９：
Ｆｅ４７．１−Ｃｒ３４．９−Ｎｉ５．２４−Ｍｏ１０−Ａｌ２．７ｗｔ％からなる成分組成の混合物を金属触媒として用いて、本発明例１と同様な方法で４．２ＧＰａ，１３００℃で１時間反応させたところ、全体に多量のｃＢＮ粒子が生成した。平均粒子径は約０．５ｍｍのｃＢＮ粒子であった。
Invention Example 9:
Using a mixture of component composition consisting of Fe47.1-Cr34.9-Ni5.24-Mo10-Al2.7 wt% as a metal catalyst, reaction was conducted at 4.2 GPa and 1300 ° C. for 1 hour in the same manner as in Example 1 of the present invention. As a result, a large amount of cBN particles was generated as a whole. The average particle size was cBN particles of about 0.5 mm.
本発明例１０：
Ｆｅ３４−Ｃｏ１７−Ｃｒ３２．４−Ｍｏ１４．２−Ａｌ２．４ｗｔ％からなる成分組成の混合物を金属触媒として用いて、本発明例１と同様な方法で４．２ＧＰａ，１３００℃で１時間反応させたところ、全体に多量のｃＢＮ粒子が生成した。平均粒子径は約０．３ｍｍのｃＢＮ粒子であった。
Invention Example 10:
Using a mixture of component composition consisting of Fe34-Co17-Cr32.4-Mo14.2-Al2.4 wt% as a metal catalyst, the mixture was reacted at 4.2 GPa at 1300 ° C. for 1 hour in the same manner as in Example 1 of the present invention. However, a large amount of cBN particles was generated overall. The average particle diameter was cBN particles of about 0.3 mm.
本発明例１１：
Ｃｏ４８．７−Ｃｒ１６．２−Ｍｏ３２．４−Ａｌ１２．７ｗｔ％からなる成分組成の混合物を金属触媒として用いて、本発明例１と同様な方法で４．２ＧＰａ，１３００℃で１時間反応させたところ、全体に多量のｃＢＮ粒子が生成した。平均粒子径は約０．３ｍｍのｃＢＮ粒子であった。本実施例は特にＣｒに対して、Ｍｏが過剰な成分を選択したために、Ｃｒが過剰な成分を有する触媒に比べて、若干ｃＢＮの収率が低下していた。
Invention Example 11:
Co 48.7-Cr16.2-Mo32.4-Al 12.7 wt% of the composition of the component composition was used as a metal catalyst, and reacted at 4.2 GPa and 1300 ° C. for 1 hour in the same manner as in Example 1 of the present invention. However, a large amount of cBN particles was generated overall. The average particle diameter was cBN particles of about 0.3 mm. In this example, since a component having an excessive amount of Mo with respect to Cr was selected, the yield of cBN was slightly reduced as compared with a catalyst having an excessive component of Cr.
本発明例１２：
Ｃｏ３８．５−Ｆｅ１９．２−Ｃｒ２８．８−Ｍｏ９．６１−Ａｌ３．８５ｗｔ％からなる成分組成の混合粉末を金属触媒として用い、本発明例１と同様な方法で、４．４ＧＰａ、１４１３℃で１時間反応させたところ、８０％以上のｈＢＮが均質な約０．１〜０．２ｍｍのｃＢＮ粒子に転換していた。
Invention Example 12:
Co 38.5-Fe 19.2-Cr 28.8-Mo 9.61-Al 3.85 wt% mixed powder having a component composition was used as a metal catalyst in the same manner as in Example 1 of the present invention at 4.4 GPa at 1413 ° C. When reacted for 1 hour, 80% or more of hBN was converted into homogeneous cBN particles of about 0.1 to 0.2 mm.
比較例４：
本発明例１２の上記金属触媒において、ＭｏとＣｒの含有割合を増加し、Ｃｏ１８．２−Ｆｅ１９．２−Ｃｒ２８．３−Ｍｏ３１．２−Ａｌ３．１ｗｔ％からなる成分組成の混合粉末からなる金属触媒を作製し、本発明例１２と同様に、４．４ＧＰａ、１４１３℃で１時間反応させたところ、ｃＢＮは生成しなかった。ＣｒとＭｏの合計含有割合が５５ｗｔ％以上であるため、金属触媒の融点が高くなったことによるものと考えられる。ちなみに、この処理条件はｃＢＮが安定な領域内と考えられる。
よって、ＣｒとＭｏの合計含有割合を５５ｗｔ％以下にすることが必要である。
Comparative Example 4:
In the above metal catalyst of Invention Example 12, the content of Mo and Cr is increased, and the metal is composed of a mixed powder having a component composition of Co18.2—Fe19.2—Cr28.3—Mo31.2—Al3.1 wt%. When a catalyst was prepared and reacted at 4.4 GPa and 1413 ° C. for 1 hour as in Inventive Example 12, cBN was not produced. Since the total content ratio of Cr and Mo is 55 wt% or more, it is considered that the melting point of the metal catalyst is increased. Incidentally, this processing condition is considered to be in a region where cBN is stable.
Therefore, it is necessary to make the total content ratio of Cr and Mo 55% by weight or less.
本発明例１３：
Ｃｏ２０−Ｆｅ４０−Ｃｒ３８−Ａｌ２ｗｔ％からなる成分組成の混合粉末を金属触媒として用い、本発明例１と同様な方法で、４．４ＧＰａ、１４００℃で１時間、また、４．２ＧＰａ、１３４０℃で１時間反応させたところ、７０％以上のｈＢＮがｃＢＮ粒子に転換していた。
Invention Example 13:
Using a mixed powder having a component composition of Co20-Fe40-Cr38-Al2 wt% as a metal catalyst, in the same manner as in Example 1 of the present invention, at 4.4 GPa and 1400 ° C. for 1 hour, and at 4.2 GPa and 1340 ° C. When reacted for 1 hour, 70% or more of hBN was converted to cBN particles.
上記本発明例１〜１３及び比較例１〜４を表にまとめると、表１の通りとなる。 The invention examples 1 to 13 and comparative examples 1 to 4 are summarized in the table as shown in Table 1.
上記のとおり、本発明のｃＢＮ合成方法およびｃＢＮを原料粉末とするｃＢＮ焼結体の製造方法によれば、金属触媒として、Ｎを溶解する作用を有する１５ｗｔ％以上５５ｗｔ％以下のＣｒ，Ｍｏ（但し、Ｍｏは、１５ｗｔ％≦（Ｃｒ＋Ｍｏ）≦５５ｗｔ％、かつ、Ｍｏ≦１０ｗｔ％を満足する）と、ｃＢＮ核発生・成長の促進・助長作用を有する１．５〜８ｗｔ％のＡｌ，Ｍｇと、残部はＢを溶解する作用を有するＦｅ，Ｃｏ，Ｎｉ（但し、Ｎｉは、２２ｗｔ％以下）からなる合金粉末あるいは混合粉末を用いることによって、従来よりも低圧力範囲（最低圧力４ＧＰａ）でｃＢＮを合成することができ、また、上記金属触媒と同一成分組成の焼結助剤を用いた焼結により、ｃＢＮ粒子間で強固な直接結合を有し、緻密な組織を備え高硬度を有するＢＮ焼結体を製造することができる。
As described above, according to the cBN synthesis method of the present invention and the cBN sintered body production method using cBN as a raw material powder, 15 wt% or more and 55 wt% or less of Cr, Mo (having an action of dissolving N as a metal catalyst ( However, Mo satisfies 15 wt% ≦ (Cr + Mo) ≦ 55 wt% and Mo ≦ 10 wt%), and 1.5 to 8 wt% Al, Mg having cBN nucleation / growth promotion / promotion effect The balance is cBN in a lower pressure range (
１，１１ ：グラファイトヒーター
２ ：Ｍｏ箔
３ ：金属触媒
４ ：ｈＢＮ
５，１５ ：ＮａＣｌ−１０ｗｔ％ＺｒＯ２
１２ ：ｃＢＮ＋焼結助剤（＝金属触媒）
１３ ：Ｍｏ箔
１４ ：ＷＣ／Ｃｏ
1, 11: Graphite heater 2: Mo foil 3: Metal catalyst 4: hBN
5,15: NaCl-10 wt% ZrO 2
12: cBN + sintering aid (= metal catalyst)
13: Mo foil 14: WC / Co
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102731097A (en) * | 2011-03-30 | 2012-10-17 | 三菱综合材料株式会社 | Synthesis method of cubic boron nitride and preparation method of cubic boron nitride sintered body |
| JP2014084268A (en) * | 2012-10-26 | 2014-05-12 | Sumitomo Electric Hardmetal Corp | Cubic boron nitride sintered compact and method for producing the same |
| CN103924288A (en) * | 2014-04-01 | 2014-07-16 | 许斌 | Method for preparing cubic boron nitride monocrystal micro powder by using magnesium-based compound catalyst and application of cubic boron nitride monocrystal micro powder |
| CN108176329A (en) * | 2017-12-22 | 2018-06-19 | 郑州中南杰特超硬材料有限公司 | A kind of synthetic method of cubic boron nitride |
| CN113620711A (en) * | 2021-08-26 | 2021-11-09 | 江西宁新新材料股份有限公司 | Graphite high-thermal-conductivity film and preparation method thereof |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102731097A (en) * | 2011-03-30 | 2012-10-17 | 三菱综合材料株式会社 | Synthesis method of cubic boron nitride and preparation method of cubic boron nitride sintered body |
| JP2014084268A (en) * | 2012-10-26 | 2014-05-12 | Sumitomo Electric Hardmetal Corp | Cubic boron nitride sintered compact and method for producing the same |
| US9487449B2 (en) | 2012-10-26 | 2016-11-08 | Sumitomo Electric Hardmetal Corp. | Cubic boron nitride sintered body and method for manufacturing the same |
| CN103924288A (en) * | 2014-04-01 | 2014-07-16 | 许斌 | Method for preparing cubic boron nitride monocrystal micro powder by using magnesium-based compound catalyst and application of cubic boron nitride monocrystal micro powder |
| CN103924288B (en) * | 2014-04-01 | 2016-08-17 | 山东建筑大学 | Use the cubic boron nitride monocrystal micropowder preparation method and application of magnesio composite catalyst |
| CN108176329A (en) * | 2017-12-22 | 2018-06-19 | 郑州中南杰特超硬材料有限公司 | A kind of synthetic method of cubic boron nitride |
| CN113620711A (en) * | 2021-08-26 | 2021-11-09 | 江西宁新新材料股份有限公司 | Graphite high-thermal-conductivity film and preparation method thereof |
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