JPH0321518B2 - - Google Patents
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- Publication number
- JPH0321518B2 JPH0321518B2 JP60056478A JP5647885A JPH0321518B2 JP H0321518 B2 JPH0321518 B2 JP H0321518B2 JP 60056478 A JP60056478 A JP 60056478A JP 5647885 A JP5647885 A JP 5647885A JP H0321518 B2 JPH0321518 B2 JP H0321518B2
- Authority
- JP
- Japan
- Prior art keywords
- thin film
- carbon
- reaction tube
- carbon thin
- benzene
- 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.)
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- Carbon And Carbon Compounds (AREA)
Description
【発明の詳細な説明】
<産業上の利用分野>
本発明は、比較的低温の熱分解化学気相堆積法
(熱分解CVD法)により高配向性を有する黒鉛構
造を有する炭素薄膜を製造する方法に関し、特定
の炭化水素を出発物質とし、単結晶基板を用い
て、金属光沢を呈する一様平坦な炭素堆積物を基
板上に成長させる技術であつて、新規な機能素子
を創作する上で有用な基本材料製造技術を確立し
たものである。[Detailed Description of the Invention] <Industrial Application Field> The present invention produces a carbon thin film having a highly oriented graphite structure by a relatively low-temperature pyrolytic chemical vapor deposition method (pyrolytic CVD method). Regarding the method, it is a technique that uses a specific hydrocarbon as a starting material and uses a single crystal substrate to grow a uniformly flat carbon deposit with metallic luster on the substrate, and is useful for creating new functional devices. This established a useful basic material manufacturing technology.
<従来の技術とその問題点>
化学的に安定で、3000℃以上の高温まで相変態
せず、熱と電気の伝導性に関して著しい異方性を
有する黒鉛に人工合成には、通常長期間に亘る高
温高圧の製造プロセスが必要とされた。例えば、
メタン出発物質とする場合には高温(約2000℃以
上)で熱分解しさらに高配向化する目的で高温高
圧下での熱処理が用いられている。出発物質とし
て特殊な有機化合物を用い、脱水素反応、脱ハロ
ゲン化水素反応、脱炭酸反応、脱水反応等を利用
した炭素薄膜の形成法も度々用いられている。し
かしながらこの場合、炭素堆積物の高配向化が得
られず機能材料または機能素子を実現するところ
までは至つていない。高分子繊維を高温処理する
ことにより繊維状炭素を得る方法も古くから知ら
れている。この方法では、得られる材料は、構造
材料への応用については既に考えられているもの
の物理的性質が不安定で再現性が得られないため
電気的及び熱的特性(異法性)を利用した機能材
料または機能素子への応用は困難である。<Conventional technology and its problems> Artificial synthesis of graphite, which is chemically stable, does not undergo phase transformation even at high temperatures of 3000°C or higher, and has significant anisotropy in terms of thermal and electrical conductivity, usually requires a long period of time. A manufacturing process with extensive high temperatures and pressures was required. for example,
When using methane as a starting material, heat treatment at high temperature and high pressure is used to thermally decompose it at a high temperature (approximately 2000°C or higher) and to further improve orientation. Methods of forming carbon thin films using special organic compounds as starting materials and utilizing dehydrogenation reactions, dehydrohalogenation reactions, decarboxylation reactions, dehydration reactions, etc. are also frequently used. However, in this case, highly oriented carbon deposits cannot be obtained and it has not been possible to realize a functional material or a functional element. A method of obtaining fibrous carbon by treating polymer fibers at high temperatures has also been known for a long time. Although the material obtained by this method has already been considered for application as a structural material, its physical properties are unstable and reproducibility cannot be obtained, so it is necessary to utilize electrical and thermal properties (heteromorphism) Application to functional materials or functional devices is difficult.
<発明の目的>
本発明は上記従来の現状に鑑みてなされたもの
であり、異方性を利用した機能材料または機能素
子の実現を可能とするために、高配向性を有する
結晶性の良好な雇鉛構造を有する炭素薄膜を比較
的低温で製造するための方法を提供することを目
的とする。<Purpose of the Invention> The present invention has been made in view of the above-mentioned current state of the art, and is intended to enable the realization of functional materials or functional devices that utilize anisotropy. The purpose of the present invention is to provide a method for producing a carbon thin film having a lead-containing structure at a relatively low temperature.
<発明の概要>
本発明の黒鉛構造を有する炭素薄膜の製造方法
は、芳香族炭化水素または不飽和炭化水素を出発
物質とし、基板として単結晶基板を用い、比較的
低温の熱分解化学気相堆積法により炭素薄膜を製
造することを特徴とする。<Summary of the Invention> The method for producing a carbon thin film having a graphite structure according to the present invention uses an aromatic hydrocarbon or an unsaturated hydrocarbon as a starting material, uses a single crystal substrate as a substrate, and uses a relatively low-temperature pyrolysis chemical vapor phase. It is characterized by manufacturing a carbon thin film by a deposition method.
<実施例>
第1図は本発明の1実施例に用いられる炭素薄
膜生成装置のブロツク構成図である。<Example> FIG. 1 is a block diagram of a carbon thin film production apparatus used in an example of the present invention.
出発物質としては炭化水素化合物を用いること
ができるが、芳香族炭化水素または不飽和炭化水
素を用いるのが望ましく、これらは約1000℃で熱
分解される。 Although hydrocarbon compounds can be used as starting materials, it is preferred to use aromatic or unsaturated hydrocarbons, which are thermally decomposed at about 1000°C.
具体的な炭化水素名としては、ベンゼン、ビフ
エニル、アントラセン、ヘキサメチルベンゼン、
1.2−ジブロモエチレン、2−ブチン、アセチレ
ン、ジフエニルアセチレン等がある。使用した炭
化水素の種類によつて、後述する反応管への供給
方法バブラー法、蒸発法または昇華法等を用い、
毎時数ミリモル以下の一定の供給量に制御され
る。この一定量は、出発物質の種類に強く依存す
る。この一定値以上に供給量を設定するとスス状
炭素堆積物が生成されることになる。 Specific hydrocarbon names include benzene, biphenyl, anthracene, hexamethylbenzene,
Examples include 1,2-dibromoethylene, 2-butyne, acetylene, and diphenylacetylene. Depending on the type of hydrocarbon used, the method of supplying it to the reaction tube, such as the bubbler method, evaporation method, or sublimation method, as described below, may be used.
The supply rate is controlled at a constant rate of several millimoles or less per hour. This fixed amount is strongly dependent on the type of starting material. If the supply amount is set above this certain value, sooty carbon deposits will be generated.
炭素薄膜が生成される単結晶基板としては、シ
リコン、サフアイヤ炭化珪素(α形及びβ形)、
窒化硼素、キツシユ黒鉛、高配向黒鉛等を用い、
約1000℃の反応温度で変質しない条件を満足しな
ければならない。バブラー法では水素好ましくは
アルゴンをキヤリアガスとして使用する。第1図
はバブラー法を利用した装置構成を示している。
またこの装置では減圧CVDを行うこともできる。
この場合には炭素堆積層の膜厚を、常圧CVDの
場合と比べてより均一に実現することが可能であ
る。 Single-crystal substrates on which carbon thin films are formed include silicon, sapphire silicon carbide (α-type and β-type),
Using boron nitride, hard graphite, highly oriented graphite, etc.
It must satisfy the conditions that it does not deteriorate at a reaction temperature of approximately 1000°C. The bubbler method uses hydrogen, preferably argon, as a carrier gas. FIG. 1 shows the configuration of an apparatus using the bubbler method.
This device can also perform low-pressure CVD.
In this case, it is possible to achieve a more uniform thickness of the carbon deposit layer than in the case of atmospheric pressure CVD.
以下、製造工程に従つて説明する。 The manufacturing process will be explained below.
真空蒸留による精製操作を行なつたベンゼンが
収納されたバブル容器1内にアルゴンガス制御系
2よりアルゴンガスを供給してベンゼンをバブル
させ、パイレツクスガラス管3を介して石英反応
管4へベンゼン分子を給送する。この際バブル容
器1内の液体ベンゼンの温度を一定に保持してア
ルゴンガス流量をバブル5で調節し、ベンゼン分
子の反応管4内への供給量を毎時ミリモルに一定
制御する。一方、希釈ライン6よりアルゴンガス
を流し、反応管4へ給送される直前のガラス管3
内におけるアルゴンガス中のベンゼン分子数密度
を最適化する。反応管4には前述したシリコン等
の単結晶から成る成長用基板の載置された試料台
7が配設されており反応管4の外周囲には加熱炉
8が設けられている。この加熱炉8によつて反応
管4の成長用基板は約1000℃の温度に保持されて
いる。ベンゼン分子が反応管4内に給送されると
ベンゼン分子は反応管4内で熱分解し、成長用基
板上には金属光沢の炭素堆積物が生成される。ま
た反応管4の後方には白色板状の結晶性副生成物
が生じる。これはビフエニールであることが赤外
吸収スペクトル、DSC、ガスクロマトグラフに
より確認された。反応管4内のガスは排気パイプ
9を介して排気系10へ導出され、反応管4から
除去される。 Argon gas is supplied from the argon gas control system 2 into the bubble container 1 containing benzene that has been purified by vacuum distillation to bubble the benzene, and the benzene is transferred to the quartz reaction tube 4 via the Pyrex glass tube 3. Feed molecules. At this time, the temperature of the liquid benzene in the bubble container 1 is kept constant, the argon gas flow rate is adjusted by the bubbles 5, and the amount of benzene molecules supplied into the reaction tube 4 is controlled to be constant at millimoles per hour. On the other hand, argon gas is flowed from the dilution line 6 to the glass tube 3 just before being fed to the reaction tube 4.
Optimize the number density of benzene molecules in argon gas. A sample stage 7 on which a growth substrate made of a single crystal of silicon or the like mentioned above is mounted is disposed in the reaction tube 4, and a heating furnace 8 is provided around the outer periphery of the reaction tube 4. The growth substrate of the reaction tube 4 is maintained at a temperature of about 1000° C. by the heating furnace 8 . When the benzene molecules are fed into the reaction tube 4, the benzene molecules are thermally decomposed within the reaction tube 4, and a carbon deposit with a metallic luster is generated on the growth substrate. Further, a white plate-like crystalline byproduct is produced at the rear of the reaction tube 4. This was confirmed to be biphenyl by infrared absorption spectrum, DSC, and gas chromatography. The gas in the reaction tube 4 is led out to the exhaust system 10 via the exhaust pipe 9 and removed from the reaction tube 4.
四塩化炭素と二臭化メタンの混合溶液を使用し
た浮遊法を用いて得られた炭素堆積物の密度測定
を行なつた。その結果、該炭素堆積物の薄膜は密
度α=2.1±0.1g/cm2なる値が得られた。また赤
外線吸収実験によれば炭素堆積物中には−CH、
−CH2、−CH3の存在に基く吸収は見られないこ
とが判明した。 The density of carbon deposits obtained using a floating method using a mixed solution of carbon tetrachloride and methane dibromide was measured. As a result, the thin film of carbon deposit had a density α=2.1±0.1 g/cm 2 . Furthermore, according to infrared absorption experiments, carbon deposits contain −CH,
It was found that no absorption based on the presence of -CH 2 and -CH 3 was observed.
第2図にシリコン単結晶基板上に上記方法によ
り堆積された炭素薄膜表面のRHEEDパターンの
概略図を示す。図中、(002)、(004)、(006)は黒
鉛結晶の面指数を表わしており、回折パターンは
スポツトとなり、第3図に示す基板に石英、出発
物質にメタンを用いて上記同様にして堆積された
従来の炭素薄膜に比べて非常に良好なC軸配向性
が有していることがわかつた。 FIG. 2 shows a schematic diagram of the RHEED pattern on the surface of a carbon thin film deposited by the above method on a silicon single crystal substrate. In the figure, (002), (004), and (006) represent the plane index of graphite crystal, and the diffraction pattern becomes a spot. It was found that the C-axis orientation was much better than that of conventional carbon thin films deposited using conventional methods.
反応管4内に導入されたベンゼン分子は1000℃
前後の温度に加熱されて熱分解し、順次成長用基
板上に成長形成される。この場合、成長される炭
素薄膜は成長用基板の結晶性を受け継いで良好な
結晶性を有する薄膜となり、さらに、ベンゼンは
黒鉛と同じ六員環構造を有しているために、従来
に比べて低い温度で高配向化が達成される。また
反応管4内に導入されるベンゼン分子の量は一定
に制御されているため、成長用基板に形成された
炭素堆積物の膜厚は均一となり結晶性の向上と相
俟つて金属光沢や鏡面を呈する薄膜が得られる。 Benzene molecules introduced into reaction tube 4 are at 1000℃
The material is heated to a temperature of about 100 to 100°C to thermally decompose, and is sequentially grown and formed on the growth substrate. In this case, the grown carbon thin film inherits the crystallinity of the growth substrate and becomes a thin film with good crystallinity, and since benzene has the same six-membered ring structure as graphite, it is High orientation is achieved at low temperatures. In addition, since the amount of benzene molecules introduced into the reaction tube 4 is controlled at a constant level, the thickness of the carbon deposit formed on the growth substrate is uniform, and together with improved crystallinity, it has a metallic luster and mirror surface. A thin film exhibiting this is obtained.
<発明の効果>
本発明の芳香族炭化水素または不飽和炭化水素
を出発物質とし、基板として単結晶基板を用いる
方法によれば、芳香族炭化水素または不飽和炭化
水素を出発物質とすることによる効果と単結晶基
板を用いることによる効果によつて、結晶性の良
い、高い配向性を有する異方性の黒鉛構造を有す
る炭素薄膜を比較的低温で製造することができ
る。これにより、機能電子材料への応用を促進さ
せることが期待される。<Effects of the Invention> According to the method of the present invention using an aromatic hydrocarbon or an unsaturated hydrocarbon as a starting material and using a single crystal substrate as a substrate, by using an aromatic hydrocarbon or an unsaturated hydrocarbon as a starting material, Due to this effect and the effect of using a single crystal substrate, a carbon thin film having an anisotropic graphite structure with good crystallinity and high orientation can be produced at a relatively low temperature. This is expected to promote application to functional electronic materials.
第1図は本発明の1実施例の説明に供する炭素
薄膜生成装置のブロツク構成図、第2図は実施例
による炭素薄膜表面のRHEEDパターンの概略
図、第3図は従来の炭素薄膜表面のRHEEDパタ
ーンの概略図である。
1……ベンゼン容器、2……アルゴンガス制御
系、3……ガラス管、4……反応管、6……希釈
ライン、7……試料台、8……加熱炉。
Fig. 1 is a block configuration diagram of a carbon thin film production device used to explain one embodiment of the present invention, Fig. 2 is a schematic diagram of the RHEED pattern on the surface of the carbon thin film according to the embodiment, and Fig. 3 is a schematic diagram of the RHEED pattern on the surface of the carbon thin film according to the embodiment. FIG. 2 is a schematic diagram of a RHEED pattern. 1... Benzene container, 2... Argon gas control system, 3... Glass tube, 4... Reaction tube, 6... Dilution line, 7... Sample stand, 8... Heating furnace.
Claims (1)
物質とし、基板として単結晶基板を用いて、上記
炭化水素を低温熱分解することにより、 上記単結晶基板上に化学気相堆積法により炭素
薄膜を形成することを特徴とする黒鉛構造を有す
る炭素薄膜の製造方法。[Claims] 1. Using an aromatic hydrocarbon or an unsaturated hydrocarbon as a starting material and using a single crystal substrate as a substrate, the hydrocarbon is thermally decomposed at a low temperature, thereby forming a chemical vapor phase on the single crystal substrate. A method for producing a carbon thin film having a graphite structure, the method comprising forming the carbon thin film by a deposition method.
Priority Applications (9)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60056478A JPS61222989A (en) | 1985-03-20 | 1985-03-20 | Production of carbon thin film |
| EP88113145A EP0305790B1 (en) | 1985-03-20 | 1986-03-20 | Production of graphite intercalation compound and doped carbon films |
| DE8686103833T DE3678030D1 (en) | 1985-03-20 | 1986-03-20 | MANUFACTURE OF CARBON LAYERS. |
| EP86103833A EP0201696B1 (en) | 1985-03-20 | 1986-03-20 | Production of carbon films |
| DE8888113145T DE3687529T2 (en) | 1985-03-20 | 1986-03-20 | PRODUCTION OF GRAPHITE STORAGE COMPOUND AND DOPED CARBON FILMS. |
| US07/190,353 US4946370A (en) | 1985-03-20 | 1988-05-05 | Method for the production of carbon films having an oriented graphite structure |
| US07/344,961 US5049409A (en) | 1985-03-20 | 1989-04-28 | Method for metal or metal compounds inserted between adjacent graphite layers |
| US07/706,006 US5273778A (en) | 1985-03-20 | 1991-05-28 | Method for producing graphite intercalation compound |
| US08/051,441 US5404837A (en) | 1985-03-20 | 1993-04-22 | Method for preparing a graphite intercalation compound having a metal or metal compounds inserted between adjacent graphite layers |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60056478A JPS61222989A (en) | 1985-03-20 | 1985-03-20 | Production of carbon thin film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61222989A JPS61222989A (en) | 1986-10-03 |
| JPH0321518B2 true JPH0321518B2 (en) | 1991-03-22 |
Family
ID=13028201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60056478A Granted JPS61222989A (en) | 1985-03-20 | 1985-03-20 | Production of carbon thin film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61222989A (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5927753B2 (en) * | 1981-11-25 | 1984-07-07 | 科学技術庁無機材質研究所長 | Diamond synthesis method |
-
1985
- 1985-03-20 JP JP60056478A patent/JPS61222989A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61222989A (en) | 1986-10-03 |
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