JPH02196094A - Method for synthesizing diamond by combustion flame - Google Patents
Method for synthesizing diamond by combustion flameInfo
- Publication number
- JPH02196094A JPH02196094A JP1196889A JP1196889A JPH02196094A JP H02196094 A JPH02196094 A JP H02196094A JP 1196889 A JP1196889 A JP 1196889A JP 1196889 A JP1196889 A JP 1196889A JP H02196094 A JPH02196094 A JP H02196094A
- Authority
- JP
- Japan
- Prior art keywords
- flame
- substrate
- diamond
- gas
- premixed
- 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.)
- Pending
Links
- 239000010432 diamond Substances 0.000 title claims abstract description 42
- 229910003460 diamond Inorganic materials 0.000 title claims abstract description 39
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 title claims description 18
- 230000002194 synthesizing effect Effects 0.000 title claims description 4
- 239000000758 substrate Substances 0.000 claims abstract description 31
- 239000007789 gas Substances 0.000 abstract description 22
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 19
- 239000001301 oxygen Substances 0.000 abstract description 19
- 229910052760 oxygen Inorganic materials 0.000 abstract description 19
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 abstract description 8
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 abstract description 6
- 239000000446 fuel Substances 0.000 abstract description 6
- 229910052799 carbon Inorganic materials 0.000 abstract description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 4
- 230000001590 oxidative effect Effects 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 3
- 239000007800 oxidant agent Substances 0.000 abstract description 3
- 238000010408 sweeping Methods 0.000 abstract description 3
- 239000001273 butane Substances 0.000 abstract description 2
- 125000004432 carbon atom Chemical group C* 0.000 abstract description 2
- -1 ethylene, propylene, propane Chemical class 0.000 abstract description 2
- 239000011261 inert gas Substances 0.000 abstract description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 abstract description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003345 natural gas Substances 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 description 13
- 238000003786 synthesis reaction Methods 0.000 description 9
- 239000010453 quartz Substances 0.000 description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 206010061218 Inflammation Diseases 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 230000004054 inflammatory process Effects 0.000 description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 238000001069 Raman spectroscopy Methods 0.000 description 2
- 238000001237 Raman spectrum Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- 230000001678 irradiating effect Effects 0.000 description 2
- 125000004430 oxygen atom Chemical group O* 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- UONOETXJSWQNOL-UHFFFAOYSA-N tungsten carbide Chemical compound [W+]#[C-] UONOETXJSWQNOL-UHFFFAOYSA-N 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000011203 carbon fibre reinforced carbon Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 239000013626 chemical specie Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 235000012489 doughnuts Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- MWWATHDPGQKSAR-UHFFFAOYSA-N propyne Chemical group CC#C MWWATHDPGQKSAR-UHFFFAOYSA-N 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は燃焼炎を用いて大面積にわたって連続的にダイ
ヤモンドを合成する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for continuously synthesizing diamond over a large area using a combustion flame.
[従来の技術]
気相法によるダイヤモンド合成には様々な方法が知られ
ている。従来マイクロ波法、高周波法等のプラズマを用
いてダイヤモンド膜の気相成長が行われてきたが、高速
成膜、大面積化等で問題があった。これらの方法によっ
てつくられるダイヤモンド成長表面の雰囲気及び反応は
本質的に同等であると思われ、この様な考えから大気開
放系での燃焼炎中のプラズマに着目し、燃焼炎によるダ
イヤモンドの合成を可能としたとの報告もなされている
(広瀬洋−近藤紀明第35回応用物理学関係連合講演会
講演予稿集P4341988.広瀬洋−稲村伸−化学と
工業41巻9号P8401988)、この燃焼炎法は大
気開放系でのダイヤモンド合成方法であり、ラジカルや
イオンの濃度が高いのでダイヤモンドの高速合成の実現
が期待される。しかしながら燃焼炎にはダイヤモンドが
合成される内炎の外側に外炎があり、内炎で合成された
ダイヤモンドを外炎をくぐらせて取り出すと燃焼してし
まうという本質的な問題があり、火炎の断面積よりも広
い面積でのダイヤモンドの合成は不可能であり、燃焼炎
法はマイクロ波法、高周波等の方法に比べて実用的に充
分なものではなかった。[Prior Art] Various methods are known for diamond synthesis using the vapor phase method. Conventionally, diamond films have been grown in vapor phase using plasma such as microwave methods and high frequency methods, but there have been problems with high-speed film formation, large area growth, etc. It is thought that the atmosphere and reaction on the diamond growth surface created by these methods are essentially the same, and based on this idea, we focused on the plasma in the combustion flame in an open atmosphere system and investigated the synthesis of diamond using the combustion flame. It has also been reported that this combustion flame can This method is a diamond synthesis method in an open atmosphere system, and because the concentration of radicals and ions is high, it is expected to realize high-speed diamond synthesis. However, a combustion flame has an outer flame outside the inner flame where diamonds are synthesized, and there is an essential problem that if diamonds synthesized in the inner flame are taken out by passing through the outer flame, they will burn. It is impossible to synthesize diamond in an area larger than the cross-sectional area, and the combustion flame method is not as practical as methods such as the microwave method and radio frequency method.
[発明が解決しようとする課題]
本発明は燃焼炎を利用した、基板上へのダイヤモンドの
高速連続合成及び大面積合成を目的とするものである。[Problems to be Solved by the Invention] The present invention aims at high-speed continuous synthesis and large-area synthesis of diamond on a substrate using a combustion flame.
[課題を解決するための手段、作用]
本発明は予混合火炎の外炎を分離した内炎を基板に接触
させ、前記基板上にダイヤモンドを合成することを特徴
とする燃焼炎によるダイヤモンドの合成方法である。[Means for Solving the Problems, Effects] The present invention provides a method for synthesizing diamond using a combustion flame, characterized in that an inner flame from which an outer flame of a premixed flame is separated is brought into contact with a substrate, and diamond is synthesized on the substrate. It's a method.
即ち本発明は予混合火炎の外炎を分離した内炎を基板に
接触掃引させることでダイヤモンドを大面積にわたって
基板上に高速連続合成するものである。That is, the present invention is capable of high-speed continuous synthesis of diamond on a substrate over a large area by sweeping the inner flame, which is separated from the outer flame of a premixed flame, into contact with the substrate.
燃焼現象は非常に複雑で未だにどの様な素反応が進行し
ているのかは明確ではない、従ってなぜ本発明のように
酸化炎を分離して還元炎のみにした場合に大面積にわた
って高速にダイヤモンドの膜が合成できるのかは必ずし
も明確ではないが。The combustion phenomenon is very complex, and it is still not clear what kind of elementary reactions are occurring.Therefore, why is it possible to separate the oxidation flame and create only the reduction flame, as in the present invention, to generate diamonds over a large area at high speed? However, it is not necessarily clear whether such a film can be synthesized.
以下のように考えられる。燃焼炎の内炎部分は予混合で
供給される酸素と原料ガスとの反応であるが、外炎部分
は燃焼気体と空気中酸素との反応が進行していて、理論
酸素量を下回る酸素比または空気比で燃焼している予混
合火炎の内炎部では、酸素が不足した還元性の雰囲気に
なっており、炭素分子や炭化水素分子が酸化されずに多
く存在しているものと考えられる。一方外炎部では周り
の空気から酸素が拡散するので酸化性雰囲気になってお
り一酸化炭素等の化学種が多く存在しているものと考え
られる。従って、燃焼雰囲気から酸素をなくすかあるい
は炎を不可性ガス等で被って空気を遮断すると、外炎が
消えて内炎のみになる。It can be considered as follows. In the inner flame part of the combustion flame, there is a reaction between the premixed oxygen supplied and the raw material gas, but in the outer flame part, the reaction between the combustion gas and oxygen in the air is progressing, and the oxygen ratio is lower than the theoretical oxygen amount. Alternatively, in the inner flame of a premixed flame that burns at an air ratio, there is a reducing atmosphere lacking oxygen, and it is thought that many carbon and hydrocarbon molecules exist without being oxidized. . On the other hand, in the outer flame part, oxygen diffuses from the surrounding air, resulting in an oxidizing atmosphere, and it is thought that many chemical species such as carbon monoxide are present. Therefore, if oxygen is removed from the combustion atmosphere or if the flame is covered with an inert gas or the like to block the air, the outer flame disappears and only the inner flame remains.
スミセルの分離装置(Smithells、A、& I
ngle、)1.。Smithells separation apparatus (Smithells, A, & I
ngle, )1. .
Trans、Chemi、Soc、、61.20418
92)を用いれば予混合火炎の内円錐炎と外円錐炎とを
分離することが可能である。予混合火炎とは、可燃性気
体と気体酸化剤とを予め混合してから燃焼する場合に形
成される火炎であり、予混合気体は点火源があれば空気
を遮断しても予混合気体同士が反応して燃焼する。この
火炎面に向かって予混合気体を適当な速さで移動させる
と火炎は静止して保たれる。これがスミセルの分離装置
の内円錐炎すなわち内炎ができる原理である。Trans, Chemi, Soc, 61.20418
92), it is possible to separate the inner conical flame and the outer conical flame of the premixed flame. A premixed flame is a flame that is formed when a flammable gas and a gaseous oxidizer are mixed in advance and then combusted. reacts and burns. If the premixed gas is moved toward this flame front at an appropriate speed, the flame will remain stationary. This is the principle behind the formation of the inner conical flame, or inner flame, of the Sumicelle separation device.
この燃焼の段階では、予混合気体は燃料の方が多いので
反応しなかった燃料が残っており、この燃焼気体はさら
に空気中の酸素と反応して拡散炎を形成する。これがス
ミセルの分離装置の外円錐炎すなわち外炎ができる原理
である。At this stage of combustion, the premixed gas contains more fuel, so unreacted fuel remains, and this combustion gas further reacts with oxygen in the air to form a diffusion flame. This is the principle behind the formation of the outer conical flame, or outer flame, of the Sumicelle separation device.
本発明では大面積合成のために基板に内炎を照射しなが
ら基板または内炎を移動させる必要上。In the present invention, for large-area synthesis, it is necessary to move the substrate or the inner flame while irradiating the substrate with the inner flame.
外炎を内炎から分離することが有効であることを見いだ
した。外炎を内炎から分離するためには。We found that it is effective to separate external inflammation from internal inflammation. To separate external inflammation from internal inflammation.
予混合で供給される気体酸化剤以外に燃焼炎への気体酸
化剤の供給を防げばどの様な方法でも良く、特に予混合
火炎を非酸化雰囲気の空間に吹き込む方法と、予混合火
炎を不活性ガスで覆う方法とが有効である。Any method can be used as long as it prevents the supply of gaseous oxidizers other than the gaseous oxidizer supplied by premixing to the combustion flame. In particular, there are two methods: one in which the premixed flame is blown into a space with a non-oxidizing atmosphere, and the other in which the premixed flame is prevented from being supplied to the combustion flame. A method of covering with active gas is effective.
本発明の予混合火炎の原料として用いる燃料気体として
は、炭素原子を含み火炎温度が2000℃以上のもので
あればよい、酸化気体が酸素である場合には燃料気体と
してアセチレン、エチレン、プロピレン、プロパン、ブ
タン、メチルアセチレン。The fuel gas used as a raw material for the premixed flame of the present invention may be one containing carbon atoms and having a flame temperature of 2000°C or higher. When the oxidizing gas is oxygen, the fuel gas may be acetylene, ethylene, propylene, Propane, butane, methylacetylene.
LPガス、都市ガス、天然ガスやこれらの混合ガスが使
用できる。中でも火炎温度が最も高くなるアセチレンが
望ましい、燃料の完全燃焼に必要な酸素または空気の量
は理論酸素量あるいは理論空気量と呼ばれ、実際に予混
合時に混ぜる酸素または空気の量は酸素比または空気比
と呼ばれるが、本発明においては酸素比及び空気比は、
下限が可燃下限界以上、上限が理論酸素量および理論空
気量以下の燃料過剰の範囲で、火炎温度が約2000℃
以上になる範囲であればよい0以上の範囲の中で、酸素
比及び空気比が低くなるとダイヤモンドの生成速度は早
くなるものの結晶化度が低下する。LP gas, city gas, natural gas, and a mixture of these gases can be used. Among them, acetylene is preferred because it has the highest flame temperature.The amount of oxygen or air required for complete combustion of the fuel is called the theoretical oxygen amount or theoretical air amount, and the actual amount of oxygen or air mixed during premixing is determined by the oxygen ratio or Although called the air ratio, in the present invention, the oxygen ratio and air ratio are
The flame temperature is approximately 2000℃ in the range of excess fuel where the lower limit is above the lower flammability limit and the upper limit is below the theoretical oxygen amount and theoretical air amount.
Within the range of 0 or more, the lower the oxygen ratio and the air ratio, the faster the diamond formation rate, but the lower the degree of crystallinity.
これは火炎の温度が低いためと、非ダイヤモンド成分を
エツチングする酸素原子等の励起種が、少なくなるため
であると考えられる。ダイヤモンド生成時の酸素比及び
空気比が高くなると、生成されるダイヤモンドの結晶性
は良くなるが生成速度は低下する。生成速度が低下する
のは、ダイヤモンドとなる炭素の供給量が減り、かつ酸
素原子等の励起種が増加しダイヤモンドも一部エッチン
グされるからである。This is thought to be because the flame temperature is low and the number of excited species such as oxygen atoms that etch non-diamond components is reduced. As the oxygen and air ratios increase during diamond production, the crystallinity of the produced diamond improves, but the production rate decreases. The reason why the production rate decreases is that the supply of carbon that becomes diamond decreases, and the number of excited species such as oxygen atoms increases, causing some of the diamond to be etched as well.
燃焼炎内の励起された炭素は基板に触れると急冷されて
ダイヤモンド構造に固定される。こうしてダイヤモンド
の成長が進行するので、基板は必要に応じて水等の冷媒
によって冷却するとよい。When the excited carbon in the combustion flame touches the substrate, it is rapidly cooled and fixed into the diamond structure. Since diamond growth progresses in this manner, the substrate may be cooled with a coolant such as water as necessary.
上に述べたような内炎のみからなる燃焼炎を。A combustion flame consisting only of the inner flame as described above.
ダイヤモンドが既にコーティングされである基板上に照
射すると、もとのダイヤモンドを損うことなくさらにそ
の上にダイヤモンドを合成析出させることができる。従
って本発明によって、燃焼炎を掃引することで任意の面
積の基板上に稠密に連続的にダイヤモンドを合成するこ
とが可能となった。By irradiating a substrate that is already coated with diamond, further diamond can be synthetically deposited thereon without damaging the original diamond. Therefore, according to the present invention, it has become possible to synthesize diamond continuously and densely on a substrate of any area by sweeping the combustion flame.
[実施例]
実施例1
第1図に概略を示す装置で燃焼炎によるダイヤモンドの
合成を行った。直径的10c■、高さ約10c■の石英
管1の中に、回転可能な円形の水冷台2を設置し石英管
と水冷台との隙間はシールドする。[Examples] Example 1 Diamond was synthesized using a combustion flame in an apparatus schematically shown in FIG. A rotatable circular water cooling stand 2 is installed in a quartz tube 1 having a diameter of 10 cm and a height of approximately 10 cm, and the gap between the quartz tube and the water cooling stand is shielded.
石英管の上面に、燃焼炎供給吹管火口用の孔と排気用の
孔をあけである蓋3をする。基板には表面を0.25μ
m鏡面研磨仕上げした厚さ3mm、直径8cm+のタン
グステンカーバイド板(材質旧0)4を用い水冷台の上
に設置する。A lid 3 is placed on the top surface of the quartz tube with a hole for a combustion flame supply blowpipe mouthpiece and an exhaust hole. The surface of the substrate is 0.25μ
A mirror-polished tungsten carbide plate (material: old 0) 4 with a thickness of 3 mm and a diameter of 8 cm was used and placed on a water-cooled table.
ガス溶接器(田中製作所製中型溶接器163M 、火口
100番)5にアセチレンガス2.5 m /窮in、
酸素ガス1゜5 Q /winの(0,/C2H2)比
が0.6の予混合ガスを供給して内炎の長さを30曹に
設定した後大内を下に向けて、火口を蓋3の孔から石英
管内へ挿入する。Gas welder (Tanaka Seisakusho medium size welder 163M, crater No. 100) 5 with acetylene gas 2.5 m/inch,
After supplying a premixed gas with a (0,/C2H2) ratio of 1゜5 Q/win of 0.6 and setting the length of the inner flame to 30 soybeans, turn the inner chamber downward and open the crater. Insert into the quartz tube through the hole in the lid 3.
石英管内に残存していた酸素がなくなると、外炎が消滅
する。この内炎のみからなる炎を基板の回転中心から3
cm離れたところの基板上に基板と火口の距離を2cm
に保って照射し、放射温度計による計測で基板表面温度
が800℃以上1100℃以下になるように水冷を調整
しながら、基板を1時間に1回の速さで回転させる。こ
のとき排気孔から吹き出す気体は内炎の熱で自然に発火
して拡散炎6を形成する。1時間後炎を基板から遠ざけ
て照射を終了させて基板を取り出すと、基板がドーナツ
状に切れ目なく灰色に曇り、変色帯の巾が約10■にな
った。この部分を走査電子顕微鏡で観察すると、(11
1)面と(ioo)面とにおおわれた直径約50μ璽の
ダイヤモンド粒子が稠密に存在していた。When the oxygen remaining in the quartz tube is exhausted, the external flame disappears. The flame consisting only of this inner flame is
The distance between the board and the crater is 2 cm on the board located 1 cm apart.
The substrate is rotated at a rate of once per hour while adjusting the water cooling so that the surface temperature of the substrate is 800° C. or higher and 1100° C. or lower as measured by a radiation thermometer. At this time, the gas blown out from the exhaust hole is naturally ignited by the heat of the inner flame to form a diffusion flame 6. After 1 hour, the flame was moved away from the substrate to terminate the irradiation and the substrate was taken out, and the substrate became gray and cloudy without any breaks in the shape of a doughnut, and the width of the discolored band was about 10 square meters. When this part is observed with a scanning electron microscope, (11
1) Diamond particles with a diameter of about 50 μm were densely present and covered by the (ioo) plane.
顕微ラマンでラマンスペクトルを測定すると1332C
11””に鋭いピークを示し、ダイヤモンドであること
が確認された。When the Raman spectrum is measured using a Raman microscope, it is 1332C.
It showed a sharp peak at 11'' and was confirmed to be diamond.
実施例2
第2図に概略を示す装置でダイヤモンドの合成を行った
。ガス切断器(日中製作所製切断器11C−338、火
口1番)11にシールド用ガスジャケット12を取り付
は水中切断器とした吹管に、アセチレンガス3.5 Q
/win 、酸素ガス2.4 Q /win、の(0
,/C,H,)比が0.7の予混合ガスを供給し内炎の
長さが30膳の燃焼炎とした後、シールド用ガスジャケ
ットにアルゴンガスを5 Q /win、供給すると内
炎の周囲の外炎が消滅した。基板として表面を15μ園
研磨仕上げをした厚さ5mm、幅3c園、長さ30cm
のタングステンカーバイド板(材質旧0)13を使用し
た。水中切断器の燃焼炎を下に向けて基板と火口との距
離を2cmに保ち、かつ基板の火炎が当る部分の裏側に
冷却水14を噴射する。火炎が当る部分の基板表面温度
を放射温度計による計測で800℃以上1100℃以下
に保ちながら基板を長さ方向に毎分6醜■の速さで移動
させた。40分後、基板上に幅約1 、5cm 、長さ
約25cmにわたって灰色の帯状の曇りができた。Example 2 Diamond was synthesized using an apparatus schematically shown in FIG. Attach the shielding gas jacket 12 to the gas cutter (cutter 11C-338 manufactured by Nichi Seisakusho, Crater No. 1) 11, and add acetylene gas 3.5Q to the blowpipe used as an underwater cutter.
/win, oxygen gas 2.4 Q /win, (0
, /C,H,) ratio is 0.7 to create a combustion flame with an inner flame length of 30, then argon gas is supplied to the shielding gas jacket at a rate of 5 Q/win. The outer flames around the flame disappeared. As a substrate, the surface is polished to 15 μm, thickness is 5 mm, width is 3 cm, and length is 30 cm.
A tungsten carbide plate (material: old 0) 13 was used. The combustion flame of the underwater cutter is directed downward, the distance between the substrate and the crater is maintained at 2 cm, and cooling water 14 is injected onto the back side of the part of the substrate that is hit by the flame. The substrate was moved in the length direction at a speed of 6 mm per minute while keeping the surface temperature of the substrate in the area hit by the flame at 800° C. or higher and 1100° C. or lower as measured by a radiation thermometer. After 40 minutes, a gray band of haze was formed on the substrate, about 1.5 cm wide and about 25 cm long.
この部分を走査電子顕微鏡で観察すると、(111)面
と(100)面とにおおわれた直径約10μ瓢のダイヤ
モンド粒子が稠密に存在していた。顕微ラマンでラマン
スペクトルを測定すると1332cm−”に鋭いピーク
を示し、ダイヤモンドであることが確認された。When this part was observed with a scanning electron microscope, it was found that diamond particles with a diameter of about 10 μm were densely present and covered by (111) and (100) planes. When the Raman spectrum was measured using a Raman microscope, it showed a sharp peak at 1332 cm-'', confirming that it was diamond.
[発明の効果]
本発明によりダイヤモンド粒子及びダイヤモンド多結晶
板を常圧下において高速に大面積にわたって連続的に合
成することができる。[Effects of the Invention] According to the present invention, diamond particles and diamond polycrystalline plates can be continuously synthesized over a large area at high speed under normal pressure.
第1図は本発明の実施例1で用いたダイヤモンド合成装
置の概略図、
第2図は本発明の実施例2で用いたダイヤモンド合成装
置の概略図
である。
l:石英管、 2:回転水冷台、 3:蓋、4:基板、
5:ガス溶接器、 6:拡散炎、11:ガス切断器、
12:ガスジャケット。
13:基板、 14:冷却水。FIG. 1 is a schematic diagram of a diamond synthesis apparatus used in Example 1 of the present invention, and FIG. 2 is a schematic diagram of a diamond synthesis apparatus used in Example 2 of the present invention. l: quartz tube, 2: rotating water cooling stand, 3: lid, 4: substrate,
5: Gas welder, 6: Diffusion flame, 11: Gas cutter,
12: Gas jacket. 13: Substrate, 14: Cooling water.
Claims (1)
記基板上にダイヤモンドを合成することを特徴とする燃
焼炎によるダイヤモンドの合成方法。A method for synthesizing diamond using a combustion flame, characterized in that an inner flame separated from an outer flame of a premixed flame is brought into contact with a substrate, and diamond is synthesized on the substrate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1196889A JPH02196094A (en) | 1989-01-23 | 1989-01-23 | Method for synthesizing diamond by combustion flame |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1196889A JPH02196094A (en) | 1989-01-23 | 1989-01-23 | Method for synthesizing diamond by combustion flame |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02196094A true JPH02196094A (en) | 1990-08-02 |
Family
ID=11792419
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1196889A Pending JPH02196094A (en) | 1989-01-23 | 1989-01-23 | Method for synthesizing diamond by combustion flame |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02196094A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02267193A (en) * | 1989-04-10 | 1990-10-31 | Showa Denko Kk | Method for synthesizing diamond by combustion flame method and gas burner for synthesis |
JPH04104991A (en) * | 1990-08-22 | 1992-04-07 | Japan Steel Works Ltd:The | Production of diamond and device therefor |
US5273618A (en) * | 1989-11-28 | 1993-12-28 | Showa Denko K.K. | Apparatus for vapor-phase synthesis of diamond and method for vapor-phase synthesis of diamond |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0255294A (en) * | 1988-08-18 | 1990-02-23 | Showa Denko Kk | Method for synthesizing diamond by vapor process |
JPH02188496A (en) * | 1989-01-17 | 1990-07-24 | Showa Denko Kk | Vapor-phase diamond coating method |
-
1989
- 1989-01-23 JP JP1196889A patent/JPH02196094A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0255294A (en) * | 1988-08-18 | 1990-02-23 | Showa Denko Kk | Method for synthesizing diamond by vapor process |
JPH02188496A (en) * | 1989-01-17 | 1990-07-24 | Showa Denko Kk | Vapor-phase diamond coating method |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH02267193A (en) * | 1989-04-10 | 1990-10-31 | Showa Denko Kk | Method for synthesizing diamond by combustion flame method and gas burner for synthesis |
US5273618A (en) * | 1989-11-28 | 1993-12-28 | Showa Denko K.K. | Apparatus for vapor-phase synthesis of diamond and method for vapor-phase synthesis of diamond |
JPH04104991A (en) * | 1990-08-22 | 1992-04-07 | Japan Steel Works Ltd:The | Production of diamond and device therefor |
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