JPS63188934A - Vapor growth system - Google Patents

Vapor growth system

Info

Publication number
JPS63188934A
JPS63188934A JP62021121A JP2112187A JPS63188934A JP S63188934 A JPS63188934 A JP S63188934A JP 62021121 A JP62021121 A JP 62021121A JP 2112187 A JP2112187 A JP 2112187A JP S63188934 A JPS63188934 A JP S63188934A
Authority
JP
Japan
Prior art keywords
reaction
pipe
reaction chamber
auxiliary pipe
gas
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
Application number
JP62021121A
Other languages
Japanese (ja)
Other versions
JPH0573251B2 (en
Inventor
Katsuhide Manabe
勝英 真部
Nobuo Okazaki
伸夫 岡崎
Isamu Akasaki
勇 赤崎
Kazumasa Hiramatsu
和政 平松
Hiroshi Amano
浩 天野
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.)
Nagoya University NUC
Toyoda Gosei Co Ltd
Original Assignee
Nagoya University NUC
Toyoda Gosei Co 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 Nagoya University NUC, Toyoda Gosei Co Ltd filed Critical Nagoya University NUC
Priority to JP62021121A priority Critical patent/JPS63188934A/en
Publication of JPS63188934A publication Critical patent/JPS63188934A/en
Publication of JPH0573251B2 publication Critical patent/JPH0573251B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To execute a cleaning process by only exchanging an auxiliary pipe by a method wherein the auxiliary pipe covering the upper face inside a reaction chamber is installed to be detachable in relation to the reaction chamber. CONSTITUTION:A cylindrical auxiliary pipe 40 whose cross section is like a semicircular arc is installed at a reaction chamber 20; the auxiliary pipe 40 covers the upper part of the reaction chamber 20 where a susceptor 22 is mounted; if a side plate 41 is detached, the auxiliary pipe 40 can be detached or installed after sliding the auxiliary pipe 40 on a pipe wall 21a of a quartz reaction pipe 21. Because a reaction gas and a dopant gas are introduced into a reaction chamber 25a near a sapphire substrate 24 while a first reaction-gas pipe 25 is separated from a second reaction-gas pipe 26, a reaction is restrained and a good doping process is executed. Although soot generated during the reaction process adheres to the auxiliary pipe, it is enough to exchange this auxiliary pipe for a cleaned auxiliary pipe for a cleaning process; it is easy to clean the reaction chamber.

Description

【発明の詳細な説明】[Detailed description of the invention] 【産業上の利用分野】[Industrial application field]

本発明は有機金属化合物ガスを用いた気相成長装置の使
用性を改善したものに関する。
The present invention relates to a vapor phase growth apparatus using an organometallic compound gas with improved usability.

【従来技術】[Prior art]

従来、有機金属化合物気相成長法(以下「MOVPEJ
と記す)を用いて、窒化ガリウム系化合物半導体(Aj
!x Ga+−x N ;X=0を含む)薄膜をサファ
イア基板上に気相成長させることが研究されている。 この方法は、第3図に示すような気相成長装置を用いて
実施される。その気相成長装置において、石英反応管7
にはマニホールド6が接続されており、そのマニホール
ド6には、N Hsの供給系統AとH,、N、の供給系
統Bと、有機金属化合物ガスのトリメチルガリウム(以
下rTMGJと記す)の供給系統Cと、有機金属化合物
ガスのトリメチルアルミニウム(以下rTMAJと記す
)の供給系統りと、ドーピング元素を含む反応ガス(以
下単に「ドーパントガス」という)であるジエチル亜鉛
(以下rDEZJと記す)の供給系統Eとが接続されて
いる。また、石英反応管7の中には、高周波加熱用グラ
ファイトサセプタ9が配設されており、そのサセプタ9
上にはサファイア基板10が載置されており、そのサフ
ァイア基板10は、高周波コイル8により加熱される。 各反応ガス及びキャリアガスは各供給系統からマニホー
ルド6で混合され、その混合ガスが石英反応管7に導か
れサファイア基板10に吹き付けられることによりサフ
ァイア基板10上にAlxGa+−xNの薄膜が成長す
る。 そして、各有機金属化合物ガスの混合比を変化させるこ
とにより、組成比を変化させたり、亜鉛をドープしてI
型のAl1xGal−xNの薄膜を形成することができ
る。
Conventionally, organometallic compound vapor phase epitaxy (hereinafter referred to as "MOVPEJ")
gallium nitride-based compound semiconductor (Aj
! Vapor phase growth of thin films (xGa+−xN; including X=0) on sapphire substrates has been studied. This method is carried out using a vapor phase growth apparatus as shown in FIG. In the vapor phase growth apparatus, a quartz reaction tube 7
A manifold 6 is connected to the manifold 6, and the manifold 6 has a supply system A for NHs, a supply system B for H, N, and a supply system for trimethyl gallium (hereinafter referred to as rTMGJ), an organometallic compound gas. C, a supply system for trimethylaluminum (hereinafter referred to as rTMAJ), which is an organometallic compound gas, and a supply system for diethylzinc (hereinafter, referred to as rDEZJ), which is a reactive gas containing a doping element (hereinafter simply referred to as "dopant gas"). E is connected. Further, a graphite susceptor 9 for high frequency heating is arranged inside the quartz reaction tube 7, and the susceptor 9
A sapphire substrate 10 is placed thereon, and the sapphire substrate 10 is heated by the high frequency coil 8. Reaction gases and carrier gases are mixed in a manifold 6 from each supply system, and the mixed gas is led to a quartz reaction tube 7 and blown onto a sapphire substrate 10, thereby growing a thin film of AlxGa+-xN on the sapphire substrate 10. Then, by changing the mixing ratio of each organometallic compound gas, the composition ratio can be changed, or by doping with zinc, I
A thin film of type Al1xGal-xN can be formed.

【発明が解決しようとする問題点】[Problems to be solved by the invention]

このように従来の装置では、Al1xGal−1INの
結晶成長が約1000℃という高温で行われるため、反
応ガスのTMG又はトリエチルガリウム(以下rTEG
Jと記す)が分解し、カーボン状のすすが石英反応管7
に付着し、付着したすすが結晶中に取り込まれ不純物と
して作用するという問題がある。 この問題を解決するため、従来は、石英反応管7を取り
外し、それをHF水の中に入れて洗浄していた。しかし
、石英反応管7は大きいので取り外しが煩雑であると共
に、高価であるため破損しないように細心の注意を払う
必要があった。 本発明は、上記の問題点を解決するために成されたもの
であり、その目的とするところは、気相成長装置の使用
性を改善することである。
In this way, in conventional equipment, the crystal growth of Al1xGal-1IN is performed at a high temperature of about 1000°C, so the reaction gas TMG or triethyl gallium (rTEG
(denoted as J) decomposes and carbon-like soot is produced in the quartz reaction tube 7.
There is a problem that the attached soot is incorporated into the crystal and acts as an impurity. In order to solve this problem, conventionally the quartz reaction tube 7 was removed and washed by placing it in HF water. However, since the quartz reaction tube 7 is large, it is complicated to remove it, and it is also expensive, so great care must be taken to avoid damage. The present invention was made to solve the above problems, and its purpose is to improve the usability of a vapor phase growth apparatus.

【問題点を解決するための手段】[Means to solve the problem]

上記問題点を解決するための発明の構成は、有機金属化
合物ガスを用いた気相成長装置において、反応室の内側
の少なくとも上面を覆う補助管を反応室に対し着脱自在
に設けたことである。
The structure of the invention to solve the above problem is that, in a vapor phase growth apparatus using an organometallic compound gas, an auxiliary pipe is provided that can be attached to and detached from the reaction chamber to cover at least the upper surface of the inside of the reaction chamber. .

【作用】[Effect]

反応により発生したすすは反応室の少なくとも上面を覆
う補助管に付着する。この補助管は反応室に対し着脱自
在に設けられているので、反応室の洗浄に際しては、こ
の補助管のみを取り換えれば良い。この補助管は石英反
応管に比べて小さく構成できるので着脱が簡単になる。 また、新しい補助管と取り替えるだけで直ぐに次の結晶
成長を行うことができるので、製造効率も向上する。
The soot generated by the reaction adheres to the auxiliary pipe that covers at least the upper surface of the reaction chamber. Since this auxiliary tube is detachably attached to the reaction chamber, only this auxiliary tube needs to be replaced when cleaning the reaction chamber. This auxiliary tube can be made smaller than the quartz reaction tube, so it can be easily attached and detached. Further, since the next crystal growth can be performed immediately by simply replacing the auxiliary tube with a new one, manufacturing efficiency is also improved.

【実施例】【Example】

以下、本発明を具体的な実施例に基づいて説明する。第
1図は本発明゛の具体的な一実施例に係る気相成長装置
の構成を示した断面図である。円形の石英反応管21で
囲われた反応室20では、サセプタ22が操作棒23に
支持されており、そのサセプタ22は操作棒23によっ
て位置の調整が行われる。また、サセプタ22の主面に
はサファイア基板24が配設されている。尚、8は高周
波コイルであり、サファイア基板24を加熱するための
ものである。 一方、反応室20のガスの流入側には、第1反応ガス管
25と第2反応ガス管26とが配設されている。第1反
応ガス管25は第2反応ガス管26と同心状に、第2反
応ガス管26の内部に配設されている。その第1反応ガ
ス管25は第1マニホールド27に接続され、第2反応
ガス管26は第2マニホールド28に接続されている。 そして、第17二ホールド27にはNH,の供給系統H
とキャリアガスの供給系統IとTMGの供給系統JとT
MAの供給系統にとが接続され、第2マニホールド28
にはキャリアガスの供給系統IとDEZの供給系統り止
が接続されている。 また、反応室20には、断面が半円弧状で筒状をした補
助管40が配設されている。その補助管40は第2図に
示すように底部40aと40bが石英反応管21の管壁
21aに当接し、管壁21aにより支持されている。補
助管40はサセプタ22の載置されている反応室20の
上部を覆っている。そして、側板41を取り外し、補助
管40を石英反応管21の管壁21a上をスライドさせ
て、取り外したり反応室20に設置したりすることがで
きる。 このような装置構成により、第1反応ガス管25の開口
部25aから、N HsとTMGとTMAとH3との混
合ガスが反応室20に流出し、第2反応ガス管26の開
口部26aから、DEZ(!:H2との混合ガスが反応
室20に流出する。 N型のA l、lG a +−x NU膜を形成する場
合には、第1反応ガス管25だけから混合ガスを流出さ
せれば良、く、■型のAβxGa’+−xN薄膜を形成
する場合には、第1反応ガス管25と第2反応ガス管2
6とからそれぞれの混合ガスを流出させれば良い。■型
のAlXGaI−XN′R膜を形成する場合には、ドー
パントガスであるDEZは第1反応ガス管25から流出
する反応ガスとサファイ子基板24の近辺の反応室20
aで初めて混合されることになる。そして、DEZはサ
ファイア基板24に吹き付けられ熱分解し、ドーパント
元素は成長するAlxGa+−xNにドーピングされて
、■型のAj!xGa1−xNが得られる。この場合、
第1反応ガス管25と第2反応ガス管26とで分離して
、反応ガスとドーパントガスがサファイア基板24の付
近の反応室25aまで導かれるので、従来装置で生じる
ガスの導入管におけるDEZとTMG又はTMAとの反
応が抑制されるため、良好なドーピングが行われる。 尚、サセプタ22の反応ガスの流れる方向Xに対する傾
斜角θは、45度に構成されている。このように傾斜さ
せることにより、サセプタ22をガス流に対し直角に構
成した場合に比べて良好な結晶が得られた。 又、開口部25a、26aとサファイア基板24との間
隔は、10〜60mmに制御棒23により調整されるの
が望ましい。 又、上記の実施例では、第1反応管と第2反応管とを設
はドーパントガスを他の反応ガスと混合することなく、
サファイア基板24の近辺まで導入しており、■型のA
j!xGa+−xNの結晶性が向上するが、この効果を
生じさせなくても良い場合には、従来装置のように予め
マニホールドでドーパントガスを他の反応ガスと混合し
た上で反応室に導き、傾斜したサファイア基板24の主
面24aに吹き付けてもよい。 このような装置で、良質のAji!xGa+−xN薄膜
を気相成長させることができる。補助管40にすすが付
着した場合には、側板41を取り外して中の補助管40
を取り出し、他の洗浄された補助管と交換すれば、直ち
に次の結晶成長を行うことができる。
The present invention will be described below based on specific examples. FIG. 1 is a sectional view showing the structure of a vapor phase growth apparatus according to a specific embodiment of the present invention. In a reaction chamber 20 surrounded by a circular quartz reaction tube 21, a susceptor 22 is supported by an operating rod 23, and the position of the susceptor 22 is adjusted by the operating rod 23. Further, a sapphire substrate 24 is disposed on the main surface of the susceptor 22. Note that 8 is a high frequency coil for heating the sapphire substrate 24. On the other hand, on the gas inflow side of the reaction chamber 20, a first reaction gas pipe 25 and a second reaction gas pipe 26 are arranged. The first reaction gas pipe 25 is arranged concentrically with the second reaction gas pipe 26 inside the second reaction gas pipe 26 . The first reaction gas pipe 25 is connected to a first manifold 27 , and the second reaction gas pipe 26 is connected to a second manifold 28 . The 17th second hold 27 has a supply system H for NH.
and carrier gas supply system I and TMG supply system J and T
is connected to the MA supply system, and the second manifold 28
A carrier gas supply system I and a DEZ supply system stop are connected to. Further, an auxiliary tube 40 having a cylindrical shape and a semicircular arc cross section is disposed in the reaction chamber 20. As shown in FIG. 2, the auxiliary tube 40 has its bottom portions 40a and 40b in contact with the tube wall 21a of the quartz reaction tube 21, and is supported by the tube wall 21a. The auxiliary pipe 40 covers the upper part of the reaction chamber 20 in which the susceptor 22 is placed. Then, by removing the side plate 41 and sliding the auxiliary tube 40 on the tube wall 21a of the quartz reaction tube 21, it can be removed or installed in the reaction chamber 20. With such an apparatus configuration, a mixed gas of NHs, TMG, TMA, and H3 flows into the reaction chamber 20 from the opening 25a of the first reaction gas pipe 25, and flows out from the opening 26a of the second reaction gas pipe 26. , DEZ(!: H2 flows out into the reaction chamber 20. When forming an N-type Al,lG a +-x NU film, the mixed gas flows out only from the first reaction gas pipe 25. In the case of forming a type AβxGa'+-xN thin film, the first reaction gas pipe 25 and the second reaction gas pipe 2 may be
It is sufficient if the respective mixed gases are allowed to flow out from 6 and 6. In the case of forming a type (2) type Al
It will be mixed for the first time in a. Then, DEZ is sprayed onto the sapphire substrate 24 and thermally decomposed, and the dopant element is doped into the growing AlxGa+-xN to form ■-type Aj! xGa1-xN is obtained. in this case,
Since the reaction gas and the dopant gas are separated by the first reaction gas pipe 25 and the second reaction gas pipe 26 and guided to the reaction chamber 25a near the sapphire substrate 24, the DEZ in the gas introduction pipe that occurs in the conventional device is Since the reaction with TMG or TMA is suppressed, good doping is achieved. Incidentally, the inclination angle θ of the susceptor 22 with respect to the flow direction X of the reaction gas is set to 45 degrees. By tilting the susceptor 22 in this manner, better crystals were obtained than when the susceptor 22 was configured perpendicular to the gas flow. Further, it is desirable that the distance between the openings 25a, 26a and the sapphire substrate 24 be adjusted to 10 to 60 mm using the control rod 23. In addition, in the above embodiment, the first reaction tube and the second reaction tube are set so that the dopant gas is not mixed with other reaction gases.
It is introduced up to the vicinity of the sapphire substrate 24, and the ■ type A
j! The crystallinity of xGa+-xN improves, but if this effect does not need to be produced, the dopant gas is mixed with other reaction gases in a manifold in advance and introduced into the reaction chamber, as in conventional equipment, and then tilted. It may also be sprayed onto the main surface 24a of the sapphire substrate 24. With such a device, you can get high quality Aji! xGa+-xN thin films can be grown in vapor phase. If soot adheres to the auxiliary pipe 40, remove the side plate 41 and remove the auxiliary pipe 40 inside.
If you take it out and replace it with another cleaned auxiliary tube, you can immediately start growing the next crystal.

【発明の効果】【Effect of the invention】

本発明は有機金属化合物ガスを用いた気相成長装置にお
いて、反応室の内側の少なくとも上面を覆う補助管を反
応室に対し着脱自在に設けているので、反応過程で発生
したすすは補助管に付着し、洗浄時にはこの補助管を他
の洗浄された補助管に交換すればよく、反応室の洗浄が
容易に行われるという効果がある。
In a vapor phase growth apparatus using organometallic compound gas, the present invention is provided with an auxiliary tube that covers at least the upper surface of the inside of the reaction chamber and is detachable from the reaction chamber, so that the soot generated during the reaction process is removed from the auxiliary tube. At the time of cleaning, this auxiliary tube can be replaced with another cleaned auxiliary tube, which has the effect of facilitating cleaning of the reaction chamber.

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

第1図は本発明の具体的な一実施例に係る気相成長装置
の構成を示した構成図。第2図はその装置における反応
室の断面図。第3図は従来の気相成長装置の構成を示し
た構成図である。 7・・・石英反応管 8・−゛高周波コイル 9°・・
サセプタ 10・・・・サファイア基板 20・・・・
反応室 21゛゛石英反応管 22゛・・サセプタ 2
3°・“制御棒24・・・・サファイア基板 25・・
・・第1反応ガス管26・・・°第2反応ガス管 27
・・・第1マニホールド 28・・・・第2マニホール
ド 40・・・・補助管 41 ・側壁 Ho・”NH
sの供給系統 Io・・°キャリアガスの供給系統 J
・・・TMGの供給系統 K・・・・TMAの供給系統
 L・・・・DEZの供給系統特許出願人  豊田合戊
株式会社 同  名古屋大学長
FIG. 1 is a configuration diagram showing the configuration of a vapor phase growth apparatus according to a specific embodiment of the present invention. FIG. 2 is a sectional view of the reaction chamber in the device. FIG. 3 is a block diagram showing the structure of a conventional vapor phase growth apparatus. 7...Quartz reaction tube 8...High frequency coil 9°...
Susceptor 10...Sapphire substrate 20...
Reaction chamber 21゛゛Quartz reaction tube 22゛...Susceptor 2
3°・“Control rod 24...Sapphire substrate 25...
...First reaction gas pipe 26...°Second reaction gas pipe 27
...First manifold 28...Second manifold 40...Auxiliary pipe 41 ・Side wall Ho・"NH
s supply system Io...°Carrier gas supply system J
...TMG supply system K...TMA supply system L...DEZ supply system Patent applicant Toyota Gosho Co., Ltd. President of Nagoya University

Claims (1)

【特許請求の範囲】 有機金属化合物ガスを用いた気相成長装置において、 反応室の内側の少なくとも上面を覆う補助管を反応室に
対し着脱自在に設けたことを特徴とする気相成長装置。
[Scope of Claim] A vapor phase growth apparatus using organometallic compound gas, characterized in that an auxiliary tube that covers at least the upper surface of the inside of the reaction chamber is detachably attached to the reaction chamber.
JP62021121A 1987-01-31 1987-01-31 Vapor growth system Granted JPS63188934A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62021121A JPS63188934A (en) 1987-01-31 1987-01-31 Vapor growth system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62021121A JPS63188934A (en) 1987-01-31 1987-01-31 Vapor growth system

Publications (2)

Publication Number Publication Date
JPS63188934A true JPS63188934A (en) 1988-08-04
JPH0573251B2 JPH0573251B2 (en) 1993-10-14

Family

ID=12046048

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62021121A Granted JPS63188934A (en) 1987-01-31 1987-01-31 Vapor growth system

Country Status (1)

Country Link
JP (1) JPS63188934A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0440529U (en) * 1990-08-06 1992-04-07

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0440529U (en) * 1990-08-06 1992-04-07

Also Published As

Publication number Publication date
JPH0573251B2 (en) 1993-10-14

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