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JPH0380533B2 - - Google Patents
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JPH0380533B2 - - Google Patents

Info

Publication number
JPH0380533B2
JPH0380533B2 JP58023482A JP2348283A JPH0380533B2 JP H0380533 B2 JPH0380533 B2 JP H0380533B2 JP 58023482 A JP58023482 A JP 58023482A JP 2348283 A JP2348283 A JP 2348283A JP H0380533 B2 JPH0380533 B2 JP H0380533B2
Authority
JP
Japan
Prior art keywords
solvent metal
cylindrical
diamond
crystals
solvent
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 - Lifetime
Application number
JP58023482A
Other languages
Japanese (ja)
Other versions
JPS59152214A (en
Inventor
Shuji Yatsu
Akihito Yoshida
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.)
Sumitomo Electric Industries Ltd
Original Assignee
Sumitomo Electric Industries 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 Sumitomo Electric Industries Ltd filed Critical Sumitomo Electric Industries Ltd
Priority to JP58023482A priority Critical patent/JPS59152214A/en
Publication of JPS59152214A publication Critical patent/JPS59152214A/en
Publication of JPH0380533B2 publication Critical patent/JPH0380533B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/06Processes using ultra-high pressure, e.g. for the formation of diamonds; Apparatus therefor, e.g. moulds or dies
    • B01J3/062Processes 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2203/00Processes utilising sub- or super atmospheric pressure
    • B01J2203/06High pressure synthesis
    • B01J2203/065Composition of the material produced
    • B01J2203/0655Diamond
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2203/00Processes utilising sub- or super atmospheric pressure
    • B01J2203/06High pressure synthesis
    • B01J2203/0675Structural or physico-chemical features of the materials processed
    • B01J2203/068Crystal growth

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Carbon And Carbon Compounds (AREA)

Description

【発明の詳細な説明】 (イ) 技術分野 本発明は、温度差法によるダイヤモンド合成方
法に関して、これを改良して、ダイヤモンドの収
量を増大させる方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (a) Technical Field The present invention relates to a diamond synthesis method using a temperature difference method, and relates to a method for improving the method and increasing the yield of diamond.

(ロ) 従来技術とその問題点 温度差法によるダイヤモンドの合成は通常の黒
鉛から、直接ダイヤへ変換する方法に比べ、成長
速度が遅く、それゆえ良質の大型結晶を合成する
ことが可能であるが、反面、反応容器内の空間の
うち結晶成長に適した空間が少なく、また合成時
間が長くなるため製造経費が高くなることが欠点
とされている。
(b) Conventional technology and its problems Synthesizing diamond using the temperature difference method has a slower growth rate than the method of directly converting ordinary graphite into diamond, and therefore it is possible to synthesize large crystals of good quality. However, on the other hand, the drawbacks are that there is only a small amount of space suitable for crystal growth within the reaction vessel, and that the synthesis time is long, resulting in high production costs.

従来の方法は、第1図に示すような構成の試料
をベルト型超高圧装置に入れて加圧し、円筒状発
熱体に通電して、50〜60Kb、1400〜1600℃を保
持することで試料容器内に生じる軸方向の温度差
を利用する。すなわち試料容器の軸方向中央部付
近に配置された、炭素供給源はその下部に配置さ
れた溶媒金属部に比べ高温になり、さらに溶媒金
属内の最下部すなわち最低温部に配置された種結
晶との間に20〜50℃の温度差が生じる。この温度
差が炭素の溶媒金属に対する溶解度の差となり、
これを駆動力として、炭素供給源から種結晶の方
向へ炭素の流れが生じ、種結晶上にダイヤモンド
が成長する。
The conventional method is to place a sample with the configuration shown in Figure 1 in a belt-type ultra-high pressure device, pressurize it, apply electricity to a cylindrical heating element, and maintain the sample at 50-60Kb and 1400-1600℃. Utilizes the temperature difference in the axial direction that occurs within the container. In other words, the carbon supply source placed near the axial center of the sample container has a higher temperature than the solvent metal part placed below it, and the seed crystal placed at the lowest or lowest temperature part within the solvent metal. There will be a temperature difference of 20-50℃ between the two. This temperature difference results in a difference in the solubility of carbon to the solvent metal,
Using this as a driving force, carbon flows from the carbon supply source toward the seed crystal, and diamond grows on the seed crystal.

また同様に第2図に示すように試料容器内上半
分に生じた温度差を利用することも試みられてい
るが、この方法では試料容器の上半分において
は、種結晶から成長するダイヤモンド結晶以外に
も極めて多数の自発的核発生により生じたダイヤ
モンドが生成してしまい、得られる結晶は集合体
または結晶同志が接触して応力集中が起り、へき
開によつて亀裂、破壊の生じたものとなり、良質
の大型単結晶ダイヤモンドを合成することは事実
上不可能である。このような現象が起こる原因と
して考えられる事項は、次の2点である。
Similarly, attempts have been made to utilize the temperature difference that occurs in the upper half of the sample container as shown in Figure 2, but in this method, the upper half of the sample container is free from diamond crystals that grow from seed crystals. However, an extremely large number of diamonds are generated due to spontaneous nucleation, and the resulting crystals are aggregates or crystals come into contact with each other, stress concentration occurs, and cracks and fractures occur due to cleavage. It is virtually impossible to synthesize large single-crystal diamonds of good quality. The following two points are possible causes of this phenomenon.

(1) 溶媒金属の下部に配置された炭素供給源で生
じた微少なダイヤモンド結晶が浮上し、溶媒金
属上部に配置された種結晶の周囲で成長する。
(1) Minute diamond crystals generated in the carbon source placed below the solvent metal float to the surface and grow around the seed crystal placed above the solvent metal.

(2) 溶媒金属中の下部に存在する炭素含有量の多
い高温溶媒の密度が上部のそれよりも小さいた
めに溶媒の対流が起こり炭素供給量が過剰とな
る。
(2) Because the density of the high-temperature solvent with a high carbon content in the lower part of the solvent metal is lower than that in the upper part, solvent convection occurs and the amount of carbon supplied becomes excessive.

(ハ) 発明の開示 本発明は前記の問題点を解決すべく研究を行な
つた結果であり、限られた反応容器内の空間を有
効に利用することを可能にする方法である。本発
明者らは従来方法の問題点が、溶媒金属と炭素供
給源との位置関係にあることを見出した。すなわ
ち従来方法は溶媒金属に対して重力方向に炭素供
給源が配置されていることで前記の問題点が生じ
るのであり、これに対して本発明は、第3図に示
すように炭素供給源を溶媒金属と円筒状発熱体の
間に配置することにより炭素供給源で生じたダイ
ヤモンド結晶が浮上するのを防止できるととも
に、炭素供給源と種結晶との高さの差が従来方法
に比べ小さいため対流が生じにくく、種結晶以外
からの自発的核発生を著しく減少させることが可
能となる。したがつて本発明によれば、従来反応
容器内の下半分の空間しか利用できなかつたもの
が、上半分も利用できるようになり、その収量は
一挙に倍増するものである。
(c) Disclosure of the Invention The present invention is the result of research conducted to solve the above-mentioned problems, and is a method that makes it possible to effectively utilize the limited space inside a reaction vessel. The present inventors have discovered that the problem with the conventional method lies in the positional relationship between the solvent metal and the carbon supply source. That is, in the conventional method, the above-mentioned problem arises because the carbon supply source is arranged in the direction of gravity with respect to the solvent metal.In contrast, in the present invention, the carbon supply source is arranged in the direction of gravity with respect to the solvent metal. By placing it between the solvent metal and the cylindrical heating element, it is possible to prevent the diamond crystals generated in the carbon source from floating, and the difference in height between the carbon source and the seed crystal is smaller than in conventional methods. Convection is less likely to occur, and spontaneous nucleation from sources other than the seed crystal can be significantly reduced. Therefore, according to the present invention, whereas conventionally only the lower half of the space within the reaction vessel could be used, the upper half can now also be used, and the yield can be doubled at once.

また結晶成長に必要な温度差は、このような方
法で充分確保できる。すなわち、円筒状発熱体の
内側の温度分布は軸方向中央部から上下へ向つて
温度が低下していくような勾配が生じていると同
時に半径方向のヒーター内側から中心軸に向つて
温度が低下していくような勾配が生じている。従
来方法はこのうち軸方向の温度差のみを利用して
いるのに対して、本発明の方法は径方向の温度差
を利用しているからである。
Further, the temperature difference necessary for crystal growth can be sufficiently ensured by such a method. In other words, the temperature distribution inside the cylindrical heating element has a gradient in which the temperature decreases from the center in the axial direction toward the top and bottom, and at the same time, the temperature decreases from the inside of the heater in the radial direction toward the central axis. There is a gradient that appears to be increasing. This is because the conventional method utilizes only the temperature difference in the axial direction, whereas the method of the present invention utilizes the temperature difference in the radial direction.

このような要件を満す超高圧装置の反応室内の
構造としては、円筒状の発熱体の内側に、外周か
ら順に、絶縁体、円筒状炭素供給源、円柱状の溶
媒金属をそれぞれ同心円状に配置し、上記溶媒金
属と、これを保持する圧力媒体との接触面に配置
した種結晶上にダイヤモンド結晶を成長させる方
法が適している。また溶媒金属とこれを保持する
圧力媒体の接触面は具体的には第3,4図に示す
通りであるが、円柱状溶媒金属を用いる場合に
は、上端面、下端面、の片側または両側の1個所
以上で本発明を実施することができる。
The structure inside the reaction chamber of an ultra-high pressure device that meets these requirements is such that an insulator, a cylindrical carbon source, and a cylindrical solvent metal are arranged concentrically inside a cylindrical heating element, in order from the outer periphery. A suitable method is to grow a diamond crystal on a seed crystal that is placed on the contact surface between the solvent metal and the pressure medium that holds it. In addition, the contact surface between the solvent metal and the pressure medium that holds it is specifically as shown in Figures 3 and 4, but when using a cylindrical solvent metal, one or both sides of the upper end surface and the lower end surface are used. The invention can be practiced at one or more locations.

さらに本発明はダイヤモンドの収量増大を目的
とするものであり、反応室内に上記のセグメント
を2組以上または、円柱状炭素供給源を用いるセ
グメントと上記のセグメントを組合わせてダイヤ
モンド結晶を成長させる方式が望ましい。
Furthermore, the present invention aims to increase the yield of diamond, and includes a method of growing diamond crystals by using two or more sets of the above-mentioned segments in a reaction chamber, or by combining a segment using a cylindrical carbon source with a segment described above. is desirable.

溶媒金属形状は円柱状が好ましく、種結晶位置
はこの溶媒金属中低温となるところすなわち溶媒
上面が好ましい。またその温度差をうまく調整す
れば下面で結晶を成長させることも可能である。
The shape of the solvent metal is preferably cylindrical, and the seed crystal position is preferably at a low temperature in the solvent metal, that is, on the top surface of the solvent. It is also possible to grow crystals on the bottom surface if the temperature difference is properly adjusted.

またこのような配置の構成体2個以上を多段に
積み、より一層収量を向上させることも可能で特
に1/5〜1/30カラツト程度の比較的小さな結晶を
合成する場合に適している。なお円柱状または円
筒状の形状は円板状または輪状であつても何らさ
しつかえない。
It is also possible to stack two or more such structures in multiple stages to further improve the yield, and is particularly suitable for synthesizing relatively small crystals of about 1/5 to 1/30 carat. Note that the cylindrical or cylindrical shape may be a disc or an annular shape.

比較例 本発明との比較のため、従来方法による実験結
果を示す。反応室の構成は第2図に示すものと
し、圧力媒体である円筒状パイロフイライト6の
内側に外径24mm、内径22mmの黒鉛円筒を発熱体と
して配置し、その内側に外径18mmのFe−50Niの
円柱を溶媒金属2,2′として、また黒鉛粉末と
ダイヤモンド砥粒の混合物の型押体3,3′を第
2図のようにそれぞれ、2個づつ上下対称となる
ように配置し、これらの周囲を圧力媒体として
NaCl4で囲み、溶媒金属2の底面および2′の上
面にあたる部分に種結晶5として35/40メツシユ
の合成ダイヤモンドをそれぞれ7個づつ埋め込ん
だ。
Comparative Example For comparison with the present invention, experimental results using a conventional method will be shown. The configuration of the reaction chamber is shown in Figure 2. A graphite cylinder with an outer diameter of 24 mm and an inner diameter of 22 mm is placed as a heating element inside a cylindrical pyrofluorite 6 that is a pressure medium, and an Fe with an outer diameter of 18 mm is placed inside the graphite cylinder with an outer diameter of 24 mm and an inner diameter of 22 mm. -50Ni cylinders were used as the solvent metals 2 and 2', and two embossed bodies 3 and 3' of a mixture of graphite powder and diamond abrasive grains were arranged vertically symmetrically as shown in Figure 2. , using the surroundings as a pressure medium
Surrounded by NaCl4, seven 35/40 mesh synthetic diamonds were each embedded as seed crystals 5 in the bottom and top surfaces of the solvent metal 2 and 2', respectively.

この構成体をガードル型超高圧装置を用いて加
圧し、55Kbの圧力を加え、次いでヒーターに通
電し、炭素供給源3,3′の温度が1500℃になる
よう加熱した。この条件を50時間保持した後加熱
を停止し、減圧後に試料を取り出したところ、下
に配置した溶媒金属2の中からは、平均113mgの
7個のダイヤモンド単結晶が得られ、それぞれ種
結晶から成長していた。これに対し、上に配置し
た溶媒からは、平均8mgの百数十個の結晶が得ら
れ、その大きさは最大のものでも21mgであり、大
部分は互に接触し集合体となつていた。
This structure was pressurized using a girdle type ultra-high pressure device to apply a pressure of 55 Kb, and then the heater was energized to heat the carbon supply sources 3 and 3' to a temperature of 1500°C. After maintaining this condition for 50 hours, heating was stopped and the sample was taken out after reducing the pressure. Seven diamond single crystals with an average weight of 113 mg were obtained from the solvent metal 2 placed below, each from a seed crystal. It was growing. On the other hand, from the solvent placed above, over a hundred crystals with an average size of 8 mg were obtained, with the largest size being 21 mg, most of which were in contact with each other and formed aggregates. .

実施例 1 第3図に示すように外径12mmのFe−50Niの溶
媒金属7の外周に内径12mm、外径18mmの円筒状の
炭素供給源型押し体8を配置し、溶媒金属の上面
に接触するNaCl4に種結晶を7個埋め込み、下
半分の構成を比較例と同一にした構成体を用い
て、比較例と同一条件の実験を行つたところ、下
側の溶媒2からは、平均102mgの7個のダイヤモ
ンド単結晶が得られ、上側の溶媒からは、平均
140mgの7個の結晶が得られた。いずれの結晶も
種結晶から成長した良質のものであり、上下どち
らの溶媒中においても自発的核発生は全く起こら
ず比較例に対して、著しい改善が見られた。
Example 1 As shown in Fig. 3, a cylindrical carbon source embossing body 8 with an inner diameter of 12 mm and an outer diameter of 18 mm was arranged around the outer periphery of a Fe-50Ni solvent metal 7 with an outer diameter of 12 mm, and a cylindrical carbon source embossing body 8 with an inner diameter of 12 mm and an outer diameter of 18 mm was placed on the upper surface of the solvent metal. When an experiment was conducted under the same conditions as the comparative example using a structure in which seven seed crystals were embedded in the contacting NaCl4 and the composition of the lower half was the same as that of the comparative example, an average of 102 mg was obtained from the lower solvent 2. 7 diamond single crystals were obtained, and from the upper solvent, the average
Seven crystals of 140 mg were obtained. All of the crystals were of good quality grown from seed crystals, and no spontaneous nucleation occurred in either the upper or lower solvent, which was a significant improvement over the comparative example.

実施例 2 第4図に示すように外径12mmのFe−50Niの溶
媒金属9,9′,9″をその間にNaCl4を入れる
よう重ね、それぞれの溶媒金属の外周に内径12
mm、外径18mmの炭素供給源型押し体8を配置し、
溶媒金属9の下面、9′の上面および下面、9″の
上面にそれぞれ7個ずつ計28個の種結晶を配置し
た構成体を用い、保持時間を20時間として、その
他の条件を比較例と同一にした実験では、計28個
の種結晶すべてから結晶が成長し、その平均は29
mgであり、計810mgの良質結晶が得られた。
Example 2 As shown in Fig. 4, Fe-50Ni solvent metals 9, 9', 9'' with an outer diameter of 12 mm are stacked so that NaCl4 is placed between them.
mm, a carbon source stamping body 8 with an outer diameter of 18 mm is arranged,
A structure in which a total of 28 seed crystals were placed on the bottom surface of solvent metal 9, the top and bottom surfaces of 9′, and the top surface of 9″ was used, the holding time was 20 hours, and other conditions were the same as in the comparative example. In the same experiment, crystals grew from all 28 seed crystals, with an average of 29
mg, and a total of 810 mg of good quality crystals were obtained.

【図面の簡単な説明】[Brief explanation of drawings]

第1図〜第4図は反応室の軸方向中央断面図
で、第1図および第2図は従来のダイヤモンド合
成方法、第3図〜第4図は本発明のダイヤモンド
合成方法の説明図である。 1:円筒状発熱体、2,2′:溶媒金属、3:
炭素供給源、4:NaCl(圧力媒体)、5:種結晶、
6:パイロフイライト(圧力媒体)、7,7′:溶
媒金属、8:円筒状炭素供給源、9,9′,9″:
溶媒金属、10,10′:溶媒金属。
Figures 1 to 4 are axial cross-sectional views of the reaction chamber, Figures 1 and 2 are explanatory diagrams of the conventional diamond synthesis method, and Figures 3 to 4 are illustrations of the diamond synthesis method of the present invention. be. 1: Cylindrical heating element, 2,2': Solvent metal, 3:
Carbon source, 4: NaCl (pressure medium), 5: Seed crystal,
6: Pyrofilite (pressure medium), 7,7': Solvent metal, 8: Cylindrical carbon source, 9,9',9'':
Solvent metal, 10,10': Solvent metal.

Claims (1)

【特許請求の範囲】 1 超高圧装置の反応室内に設置した円筒状発熱
体の内側に、外周から順に絶縁体(圧力媒体)、
円筒状炭素供給源、円柱状の溶媒金属をそれぞれ
同心円状に配置し、該円柱状溶媒金属の上端面、
下端面の片側または両面に種結晶を配置して、種
結晶上にダイヤモンド単結晶を成長させることを
特徴とするダイヤモンドの合成方法。 2 円筒状炭素供給源、円柱状の溶媒金属および
種結晶よりなるセグメントを2組以上を超高圧装
置の反応室内に配置してなることを特徴とする特
許請求の範囲第1項記載のダイヤモンドの合成方
法。
[Claims] 1. An insulator (pressure medium), an insulator (pressure medium),
A cylindrical carbon supply source and a cylindrical solvent metal are arranged concentrically, and the upper end surface of the cylindrical solvent metal,
A method for synthesizing diamond characterized by arranging a seed crystal on one or both sides of the lower end face and growing a diamond single crystal on the seed crystal. 2. The diamond according to claim 1, characterized in that two or more sets of segments each consisting of a cylindrical carbon source, a cylindrical solvent metal, and a seed crystal are arranged in a reaction chamber of an ultra-high pressure device. Synthesis method.
JP58023482A 1983-02-14 1983-02-14 Diamond synthesis method Granted JPS59152214A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58023482A JPS59152214A (en) 1983-02-14 1983-02-14 Diamond synthesis method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58023482A JPS59152214A (en) 1983-02-14 1983-02-14 Diamond synthesis method

Publications (2)

Publication Number Publication Date
JPS59152214A JPS59152214A (en) 1984-08-30
JPH0380533B2 true JPH0380533B2 (en) 1991-12-25

Family

ID=12111740

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58023482A Granted JPS59152214A (en) 1983-02-14 1983-02-14 Diamond synthesis method

Country Status (1)

Country Link
JP (1) JPS59152214A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61215293A (en) * 1985-03-15 1986-09-25 Sumitomo Electric Ind Ltd Synthesis of diamond
JPH0737549Y2 (en) * 1988-12-12 1995-08-30 アラコ株式会社 Reclining seat

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS56100122A (en) * 1980-01-14 1981-08-11 Sumitomo Electric Ind Ltd Diamond synthesizing method

Also Published As

Publication number Publication date
JPS59152214A (en) 1984-08-30

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