JPH01294598A - Vapor phase growth equipment - Google Patents
Vapor phase growth equipmentInfo
- Publication number
- JPH01294598A JPH01294598A JP12396088A JP12396088A JPH01294598A JP H01294598 A JPH01294598 A JP H01294598A JP 12396088 A JP12396088 A JP 12396088A JP 12396088 A JP12396088 A JP 12396088A JP H01294598 A JPH01294598 A JP H01294598A
- Authority
- JP
- Japan
- Prior art keywords
- vapor phase
- reaction chamber
- phase growth
- exhaust pipe
- barrel
- 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.)
- Granted
Links
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- Crystals, And After-Treatments Of Crystals (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は、熱分解反応や化学反応によって、GaAs系
、lnP系等の化合物半導体のエピタキシャル結晶、5
iOt、S+!<等の絶縁体薄膜、及び11Six、T
iSix等の導電性多結晶薄膜を気相成長する装置に関
する。Detailed Description of the Invention (Industrial Field of Application) The present invention is directed to the production of epitaxial crystals of compound semiconductors such as GaAs and lnP by thermal decomposition reactions and chemical reactions.
iOt,S+! Insulator thin film such as <, and 11Six, T
The present invention relates to an apparatus for vapor phase growth of conductive polycrystalline thin films such as iSix.
(従来の技術)
従来、気相成長装置には、バレル型サセプタを縦型反応
室に内蔵するものや、パンケーキ型サセプタを横型反応
室に内蔵するものがあり、また、加熱方式も高周波加熱
の外に抵抗加熱や赤外線加熱もある。薄膜の気相成長法
としては、原料ガスやキャリアガスにより搬送されるガ
ス状物質を反応室に導入して、熱分解反応や化学反応に
より基板上に薄膜を形成する方法がある。(Prior art) Conventionally, some vapor phase growth apparatuses have a barrel-shaped susceptor built into a vertical reaction chamber, while others have a pancake-shaped susceptor built into a horizontal reaction chamber. In addition to this, there are also resistance heating and infrared heating. As a vapor phase growth method for thin films, there is a method in which a gaseous substance carried by a source gas or a carrier gas is introduced into a reaction chamber, and a thin film is formed on a substrate by a thermal decomposition reaction or a chemical reaction.
第2図のバレル型気相成長装置を例にして以下説明する
。基板1を搭載したバレル型サセプタ2を回転軸3で反
応室4の中央に支持し、排気管5の圧力制御弁6を開放
してロータリーポンプ7により反応室を高真空に引く。A description will be given below using the barrel type vapor phase growth apparatus shown in FIG. 2 as an example. A barrel-shaped susceptor 2 carrying a substrate 1 is supported at the center of a reaction chamber 4 by a rotating shaft 3, a pressure control valve 6 of an exhaust pipe 5 is opened, and a rotary pump 7 is used to draw the reaction chamber to a high vacuum.
次いで、高周波コイル8に通電して基板Iを成長温度に
加熱してから、原料ガスを導入管9から導入し、基板1
の上に薄膜を堆積する。未反応物及び反応生成物を随伴
するガス流はバレル型サセブタ2の周囲を流下して排気
管5、圧力制御弁6及びロータリーポンプ7を経て、さ
らにダストフィルターなどを介して系外に排出される。Next, the high-frequency coil 8 is energized to heat the substrate I to the growth temperature, and then raw material gas is introduced from the introduction pipe 9 to heat the substrate 1.
deposit a thin film on top of the The gas flow accompanied by unreacted substances and reaction products flows down around the barrel-type susceptor 2, passes through an exhaust pipe 5, a pressure control valve 6, and a rotary pump 7, and is further discharged to the outside of the system via a dust filter, etc. Ru.
この圧力制御弁6は反応室4の圧力を調整するものであ
り、スロットバルブやコンダクタンスコントロールバル
ブなどが用いられる。なお、IOは冷却水を流す冷却ジ
ャケットである。This pressure control valve 6 is for adjusting the pressure in the reaction chamber 4, and a slot valve, a conductance control valve, or the like is used. Note that IO is a cooling jacket through which cooling water flows.
(発明が解決しようとする課題)
この種の気相成長装置では、未反応物や反応生成物のダ
ストがガス流に搬送されて排気管や圧力制御弁さらには
ロータリーポンプまで送られ、付着したり堆積するため
、排気系統の排気コンダクタンスが減少し、排気管が閉
塞傾向に進み、反応室の圧力を上昇させるという問題が
あった。1回の薄膜成長過程で反応室の圧力が変動する
と、例えば薄膜結晶のドーピングレベルが一定せず、電
気的光学的特性が不均一になる。(Problem to be Solved by the Invention) In this type of vapor phase growth apparatus, dust from unreacted substances and reaction products is carried by the gas flow and sent to the exhaust pipe, pressure control valve, and even the rotary pump, where it becomes attached. As a result, the exhaust conductance of the exhaust system decreases, the exhaust pipe tends to become clogged, and the pressure in the reaction chamber increases. If the pressure in the reaction chamber fluctuates during one thin film growth process, for example, the doping level of the thin film crystal will not be constant, resulting in non-uniform electrical and optical properties.
また、同様の気相成長を繰り返すと、圧力制御弁を閉塞
して反応室の圧力制御が不能となつたり、ときにはロー
タリーポンプが止まるという問題もあった。この種の問
題はバレル型気相成長装置に特有のものではなく、上記
の気相成長装置に共通するものである。Furthermore, if similar vapor phase growth is repeated, there is a problem that the pressure control valve is blocked, making it impossible to control the pressure in the reaction chamber, and sometimes causing the rotary pump to stop. This kind of problem is not unique to barrel-type vapor phase growth apparatuses, but is common to the above-mentioned vapor phase growth apparatuses.
本発明は、上記の問題を解消し、排気系統へのダストの
飛散を防+hすることにより、反応室圧力を一定に保持
することを可能とし、品質の安定した薄膜を容易に形成
することのできる気相成長装置を提供しようとするもの
である。The present invention solves the above problems, prevents dust from scattering into the exhaust system, makes it possible to maintain a constant pressure in the reaction chamber, and makes it possible to easily form a thin film with stable quality. The aim is to provide a vapor phase growth apparatus that can achieve this goal.
(課題を解決するための手段)
本発明は、基板を内部に設置する反応室と、原料ガス導
入管と、真空排気系に接続する排気管とをイTする気相
成長装置において、反応室の排気管近くにバッフル板を
設置したことを特徴とする気相成長装置である。(Means for Solving the Problems) The present invention provides a vapor phase growth apparatus in which a reaction chamber in which a substrate is installed, a raw material gas introduction pipe, and an exhaust pipe connected to a vacuum exhaust system is provided. This is a vapor phase growth apparatus characterized by a baffle plate installed near the exhaust pipe.
(作用)
第1図は、本発明の1具体例であるバレル型気相成長装
置の概念図である。この装置は、第2図の装置の排気管
5を反応室4の側壁から底部に移し、排気管5の近くに
バ・ソフル板IIを設置したものである。詳しくは、排
気管5を反応室4内に延ばし、上端を閉じた円筒状隔壁
12を排気管5に被せることにより、隔壁12と排気管
5の間に上方に向かう環状流路を形成し、該流路内にバ
ッフル板+1を設置する。なお、バレル型サセプタ2を
支持する回転軸3は隔壁I2の中央に設けた軸受13で
軸支し、カサ歯車を介して駆動軸14と接続している。(Function) FIG. 1 is a conceptual diagram of a barrel type vapor phase growth apparatus which is a specific example of the present invention. In this apparatus, the exhaust pipe 5 of the apparatus shown in FIG. 2 was moved from the side wall of the reaction chamber 4 to the bottom, and a bar-soffl plate II was installed near the exhaust pipe 5. Specifically, by extending the exhaust pipe 5 into the reaction chamber 4 and covering the exhaust pipe 5 with a cylindrical partition wall 12 with a closed upper end, an annular flow path directed upward is formed between the partition wall 12 and the exhaust pipe 5, A baffle plate +1 is installed in the flow path. Note that the rotating shaft 3 supporting the barrel-shaped susceptor 2 is supported by a bearing 13 provided at the center of the partition wall I2, and is connected to a drive shaft 14 via a bevel gear.
この装置では、バレル型2サセプタの周囲を流下する未
反応物及び反応生成物のダストが上記の環状流路を上昇
する間にバッフル板11に衝突して反応室4の底部に落
ち、捕捉される。In this device, the dust of unreacted substances and reaction products flowing down around the two barrel-shaped susceptors collides with the baffle plate 11 while rising in the annular flow path, falls to the bottom of the reaction chamber 4, and is captured. Ru.
そして、ダストを除いた清浄な排気ガスは排気管5を介
して圧力制御弁6及びロータリーポンプ7に流れるが、
ダストの付着や堆積が生じないので、排気系統の機器は
常時正確に作動し、反応室圧力の制御も確実となる。そ
の結果、−定の圧力雰囲気の下で品質の安定した薄膜を
気相成長させることが可能となる。また、第1図の装置
のように、反応室下方の環状流路にバッフル板を設け、
該流路に排気管を接続することにより、反応室内の片流
れを抑制することができ、薄膜の品質をより均一にする
ことができる。Then, the clean exhaust gas excluding dust flows through the exhaust pipe 5 to the pressure control valve 6 and the rotary pump 7.
Since there is no dust adhesion or accumulation, the exhaust system equipment always operates accurately and the reaction chamber pressure can be controlled reliably. As a result, it becomes possible to vapor phase grow a thin film with stable quality under a constant pressure atmosphere. In addition, as in the apparatus shown in Fig. 1, a baffle plate is provided in the annular flow path below the reaction chamber.
By connecting an exhaust pipe to the flow path, one-sided flow within the reaction chamber can be suppressed, and the quality of the thin film can be made more uniform.
(実施例)
第1図の装置を用いて有機金属気相成長法により、直径
3インチのGaAsウェハのヒにSiドープGaAs中
結晶をエピタキシャル成長させた。(Example) A crystal in Si-doped GaAs was epitaxially grown on a GaAs wafer having a diameter of 3 inches by metal organic vapor phase epitaxy using the apparatus shown in FIG.
まス、GaA3ウゴハをバレル型サセプタに搭載してか
ら、反応室を真空排気し、高周波コイルに通電して該ウ
ェハを成長温度の700’Cに加熱した。次いで、トリ
メチルガリウムを20secm(0’C,fatsの標
準状態における流量cm3/5in)、アルシンを1.
231.M(0℃iatmの標準状態における流In
1 /win)、シランを5scc■及び水素をキャリ
アガスとし、全流量を8 S I、Hに維持してIQT
orrの成長圧力の下で1時間エピタキシャル成長を行
った。After mounting the GaA3 wafer on a barrel-shaped susceptor, the reaction chamber was evacuated, and the high-frequency coil was energized to heat the wafer to the growth temperature of 700'C. Next, trimethyl gallium was added at a rate of 20 seconds (flow rate at 0'C, standard state of fats: cm3/5 inches), and arsine was added at a rate of 1.2 seconds.
231. M (flow In at standard conditions at 0℃iatm
1 /win), 5scc of silane and hydrogen as carrier gas, maintaining the total flow rate at 8S I,H, IQT
Epitaxial growth was performed for 1 hour under a growth pressure of orr.
1回の結晶成長で反応室の圧力変動は設定値に対して0
.5%以内で極めて安定していた。また、200回の結
晶成長終了後も、排気管や圧力制御弁に閉塞は全く認め
られず、成長室の分解清掃やメンテナンスを全く必要と
しなかった。During one crystal growth, the pressure fluctuation in the reaction chamber is 0 with respect to the set value.
.. It was extremely stable within 5%. Further, even after 200 crystal growths were completed, no clogging was observed in the exhaust pipe or pressure control valve, and no disassembly and cleaning or maintenance of the growth chamber was required.
ウェハの」―には、約2.0μIのGaAsエピタキシ
ャル層が形成されており、SIMS分析によると該層の
Si濃度分布は第3図に実線で示すように深さ方向に一
定であった。なお、深さ約2.0atl以七のSi濃度
はバックグランドレベルでアル。A GaAs epitaxial layer of about 2.0 .mu.I was formed on the wafer, and according to SIMS analysis, the Si concentration distribution in this layer was constant in the depth direction, as shown by the solid line in FIG. Note that the Si concentration at a depth of about 2.0 atl and above is at the background level.
比較のために、第2図の装置を用いてに記実施例と同様
の条件の下でSiドープGaAs単結晶のエピタキシャ
ル成長を行ったところ、1回の結晶成長で反応室の圧力
変動は設定値に対して15〜20%以上を越え、20〜
30回の結晶成長で排気管や圧力制御弁の閉塞が顕著に
なったため、成長室を分解してメンテナンス清掃を行っ
た。For comparison, epitaxial growth of a Si-doped GaAs single crystal was performed using the apparatus shown in Figure 2 under the same conditions as in the example described above, and the pressure fluctuation in the reaction chamber was reduced to the set value after one crystal growth. 15-20% or more, 20-20%
After 30 crystal growths, the exhaust pipe and pressure control valve became noticeably clogged, so the growth chamber was disassembled for maintenance and cleaning.
GaAsエピタキシャル層は、厚さが約2.0μ履であ
り、SIMS分析の結果は第3図に点線で示したように
層の深さ方向にSi′e5度勾配ができていた。The GaAs epitaxial layer had a thickness of about 2.0 .mu.m, and the results of SIMS analysis showed that a Si'e 5 degree gradient was formed in the depth direction of the layer, as shown by the dotted line in FIG.
(発明の効果)
本発明は4上記の構成を採用することにより、気相成長
過程で反応室の圧力変動を防止することができ、品質の
安定した薄膜を容易に形成することが可能となった。ま
た、圧力制御弁の操作性を改善し、装置全体のメンテナ
ンスを大幅に省略できるようになった。(Effects of the Invention) By adopting the above-mentioned configuration 4, the present invention can prevent pressure fluctuations in the reaction chamber during the vapor phase growth process, making it possible to easily form a thin film with stable quality. Ta. Additionally, the operability of the pressure control valve has been improved, making it possible to significantly reduce maintenance of the entire device.
第1図は本発明の1具体例であるバレル型気相成長装置
の概念図、第2図は従来のバレル型気相成長装置の概念
図、第3図は実施例及び比較例で得たエピタキシャル層
内のsif:5度分布を示したグラフである。Fig. 1 is a conceptual diagram of a barrel-type vapor phase growth apparatus which is a specific example of the present invention, Fig. 2 is a conceptual diagram of a conventional barrel-type vapor phase growth apparatus, and Fig. 3 is a conceptual diagram of a barrel-type vapor phase growth apparatus that is a specific example of the present invention. It is a graph showing sif:5 degree distribution in an epitaxial layer.
Claims (2)
と、真空排気系に接続する排気管とを有する気相成長装
置において、反応室の排気管近くにバッフル板を設置し
たことを特徴とする気相成長装置。(1) In a vapor phase growth apparatus that has a reaction chamber in which the substrate is installed, a raw material gas introduction pipe, and an exhaust pipe connected to the vacuum exhaust system, a baffle plate is installed near the exhaust pipe of the reaction chamber. Characteristic vapor phase growth equipment.
ガス導入管を反応室の頂部に接続し、反応室下部に上に
向かう環状流路を形成し、該流路内にバッフル板を設置
し、かつ、該流路出口に排気管を接続したことを特徴と
する特許請求の範囲(1)記載の気相成長装置。(2) A barrel-shaped susceptor is used as a substrate support, a raw material gas introduction pipe is connected to the top of the reaction chamber, an annular flow path is formed upward in the lower part of the reaction chamber, and a baffle plate is installed in the flow path. The vapor phase growth apparatus according to claim (1), further comprising an exhaust pipe connected to the outlet of the flow path.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63123960A JP2649693B2 (en) | 1988-05-23 | 1988-05-23 | Vapor phase growth equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63123960A JP2649693B2 (en) | 1988-05-23 | 1988-05-23 | Vapor phase growth equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH01294598A true JPH01294598A (en) | 1989-11-28 |
| JP2649693B2 JP2649693B2 (en) | 1997-09-03 |
Family
ID=14873596
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63123960A Expired - Fee Related JP2649693B2 (en) | 1988-05-23 | 1988-05-23 | Vapor phase growth equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2649693B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0566966U (en) * | 1992-02-21 | 1993-09-03 | ヤマハ株式会社 | Vertical heat treatment furnace |
| JP2015119041A (en) * | 2013-12-18 | 2015-06-25 | 東京エレクトロン株式会社 | Particle backflow prevention member and substrate treatment apparatus |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6289137U (en) * | 1985-11-22 | 1987-06-08 | ||
| JPS637163U (en) * | 1986-06-28 | 1988-01-18 |
-
1988
- 1988-05-23 JP JP63123960A patent/JP2649693B2/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6289137U (en) * | 1985-11-22 | 1987-06-08 | ||
| JPS637163U (en) * | 1986-06-28 | 1988-01-18 |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0566966U (en) * | 1992-02-21 | 1993-09-03 | ヤマハ株式会社 | Vertical heat treatment furnace |
| JP2015119041A (en) * | 2013-12-18 | 2015-06-25 | 東京エレクトロン株式会社 | Particle backflow prevention member and substrate treatment apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2649693B2 (en) | 1997-09-03 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |