JPH03201426A - Vapor phase molecular beam epitaxy device - Google Patents

Vapor phase molecular beam epitaxy device

Info

Publication number
JPH03201426A
JPH03201426A JP33824589A JP33824589A JPH03201426A JP H03201426 A JPH03201426 A JP H03201426A JP 33824589 A JP33824589 A JP 33824589A JP 33824589 A JP33824589 A JP 33824589A JP H03201426 A JPH03201426 A JP H03201426A
Authority
JP
Japan
Prior art keywords
raw material
exhaust gas
line
thin film
suction pump
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
Application number
JP33824589A
Other languages
Japanese (ja)
Inventor
Toshimi Aketoshi
明利 敏巳
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.)
Mitsui Kinzoku Co Ltd
Original Assignee
Mitsui Mining and Smelting 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 Mitsui Mining and Smelting Co Ltd filed Critical Mitsui Mining and Smelting Co Ltd
Priority to JP33824589A priority Critical patent/JPH03201426A/en
Publication of JPH03201426A publication Critical patent/JPH03201426A/en
Pending legal-status Critical Current

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  • Physical Deposition Of Substances That Are Components Of Semiconductor Devices (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

PURPOSE:To manufacture the title epitaxy device capable of avoiding the overshoot in case of starting the thin film deposition process as well as cutting down the times of the thin film deposition, discharging material and baking process by a method wherein a suction pump different from that provided on a deposition chamber exhaust gas line is provided in the down stream of a cold trap of a material exhaust gas line. CONSTITUTION:A suction pump comprising a mechanical booster pump 65 and a rotary pump 66 is provided in the down stream of a cold trap 52 in a material exhaust gas line (bypass line) (a). The reason why said two pumps are used is that since the deposition pressure in a deposition chamber 3 is differentiated by the kinds of formed thin films, the pressure in the material gas feed line (b) can be controlled at specific value using said two pumps in proper combination. Through these procedures, the other suction pump can be newly added to a material exhaust gas line so that the material gas feed line may keep the gas flow rate in respective pipings constant even during the material gas exhaust process.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は気相分子線エピタキシー装置に関し、詳しくは
原料供給ガスラインから系外に通じる原料排気ガスライ
ンであるバイパスラインのコールドトラップ下流に、成
長室排気ガスラインに設けられた吸引ポンプと別個に吸
引ポンプを設けた気相エピタキシー装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a gas phase molecular beam epitaxy apparatus, and more specifically, a cold trap downstream of a bypass line, which is a raw material exhaust gas line leading from a raw material supply gas line to the outside of the system, The present invention relates to a vapor phase epitaxy apparatus having a suction pump provided in a growth chamber exhaust gas line and a separate suction pump.

[従来の技術] 近年、無機薄膜、特に半導体材料を中心とした薄膜材料
の製造において、大きな変化が生じている。従来の薄膜
の製造においては、真空蒸着法、スパッタリング法、C
VD法等が知られているが、近年、有機金属をガスソー
スとし、常圧または減圧下で反応を行なう有機金属気相
成長(MOCVD)法や固体材料を原料とし、超真空下
で反応を行なう分子線エピタキシー(MBE)法が提案
されている。
[Background Art] In recent years, major changes have occurred in the production of inorganic thin films, particularly thin film materials centered on semiconductor materials. Conventional thin film manufacturing methods include vacuum evaporation, sputtering, C
The VD method is well known, but in recent years metal organic chemical vapor deposition (MOCVD), which uses an organic metal as a gas source and performs the reaction under normal pressure or reduced pressure, and the metal organic chemical vapor deposition (MOCVD) method, which uses a solid material as a raw material and performs the reaction under ultra-vacuum, have been developed. A molecular beam epitaxy (MBE) method has been proposed.

このうちMOCVD法は、常圧または減圧下で反応が行
なわれるが、成長室の圧力が比較的高いため、その場で
の結晶構造の観察ができず、薄膜の厚みの制御が行なえ
ない。また、薄膜形成を2回程度行なった後、成長室の
清掃が必要となるといった問題がある。
Among these methods, in the MOCVD method, the reaction is carried out under normal pressure or reduced pressure, but because the pressure in the growth chamber is relatively high, the crystal structure cannot be observed in situ, and the thickness of the thin film cannot be controlled. Another problem is that the growth chamber needs to be cleaned after forming a thin film about twice.

また、MBE法では、固体材料を原料とするため、原料
の再充填後、再始動に数日を要したり、得られるGa 
As等の薄膜にオーバル欠陥が生じたり、再現性良い成
長が難しいといった問題がある。また、Ga As基板
面の一部を3102等の絶縁物で覆い、Ga Asのエ
ピタキシャル成長を行なう場合に、本来結晶が付着して
は困る絶縁物上に多結晶が成長するため、好ましい選択
エピタキシャル成長ができないといった問題も生じる。
In addition, since the MBE method uses solid materials as raw materials, it may take several days to restart after refilling the raw materials, and the resulting Ga
There are problems that oval defects occur in thin films such as As and that growth with good reproducibility is difficult. In addition, when epitaxial growth of GaAs is performed by covering a part of the GaAs substrate surface with an insulator such as 3102, polycrystals grow on the insulator to which crystals should not adhere, so selective epitaxial growth is preferable. There is also the issue of not being able to do so.

このようなMOCVD法とMBE法の問題点を解決する
ため、原料の一部または全部をガスソースとする気相分
子線エピタキシー(以下、気相MBEという)法が提案
されている。また、その中でも近年、ガスソースとして
トリエチルガリウム、トリエチルアルミニウム等の有機
金属化合物を用いるMBE (MOMBE)法は、深い
不純物レベルが発生したり、オーバル欠陥等が生じるこ
とがなく、良好な結晶薄膜が得られることから、開発が
進められている。
In order to solve these problems of the MOCVD method and the MBE method, a vapor phase molecular beam epitaxy (hereinafter referred to as vapor phase MBE) method in which part or all of the raw material is used as a gas source has been proposed. In addition, in recent years, the MBE (MOMBE) method, which uses organometallic compounds such as triethylgallium and triethylaluminum as a gas source, has been developed to produce good crystalline thin films without generating deep impurity levels or oval defects. Development is progressing based on the results obtained.

このMOMBE装置の一例を第3図に示す。同図におい
て、高純度水素キャリアガスは、流量制御器11.12
において流量が制御された後、原料供給室21.22に
導入される。原料供給室21には、第■族原料であるト
リエチルアルミニウムの液体溶液が入っており、このト
リエチルアルミニウムは、液体であるため水素ガスによ
って運ばれ、流量制御器14を経て成長室3に供給され
る。同様に原料供給室22には、第■族原料であるトリ
エチルガリウムの液体溶液が入っており、水素ガスによ
って運ばれ、流量制御器15を経て成長室3に供給され
る。
An example of this MOMBE device is shown in FIG. In the same figure, high purity hydrogen carrier gas is supplied to flow controllers 11 and 12.
After the flow rate is controlled at , the raw material is introduced into the raw material supply chamber 21.22. The raw material supply chamber 21 contains a liquid solution of triethylaluminum, which is a Group Ⅰ raw material, and since this triethylaluminum is a liquid, it is carried by hydrogen gas and supplied to the growth chamber 3 via the flow rate controller 14. Ru. Similarly, the raw material supply chamber 22 contains a liquid solution of triethyl gallium, which is a Group 1 raw material, and is carried by hydrogen gas and supplied to the growth chamber 3 via the flow rate controller 15.

一方、原料供給室23に入っているアルシン(As3H
3)は気体原料なので、流量制御器13.16を経て成
長室3にそのまま供給される。この際のバルブv10〜
12は閉じている。
On the other hand, arsine (As3H) contained in the raw material supply chamber 23
Since 3) is a gaseous raw material, it is supplied directly to the growth chamber 3 via the flow rate controllers 13 and 16. At this time, the valve v10~
12 is closed.

原料供給ガスラインを経て成長室3に導入された各原料
によって、気相分子線エピタキシーによりエピタキシャ
ル薄膜が形成される。この場合には、成長室3ではAノ
Ga Asの薄膜が成長することとなる。また、Ga 
Asを成長させるにはバルブV7を閉じて、バルブVI
0.21を開くことによって系外ヘトリメチルアルミニ
ウムが放出される。この成長室3は1O−6〜10−’
T orrの圧力で薄膜の成長がなされる。
An epitaxial thin film is formed by vapor phase molecular beam epitaxy using each raw material introduced into the growth chamber 3 via the raw material supply gas line. In this case, a thin film of A-GaAs will be grown in the growth chamber 3. Also, Ga
To grow As, close valve V7 and open valve VI.
By opening 0.21, extra-system hetrimethylaluminum is released. This growth chamber 3 is 1O-6~10-'
Thin film growth is performed at a pressure of Torr.

反応後の水素ガス、エタンガス、残余原料はコールドト
ラップ5工、ターボ分子ポンプ6150−タリーポンプ
62からなる成長室排気ガスラインから系外に放出され
る。
Hydrogen gas, ethane gas, and remaining raw materials after the reaction are discharged to the outside of the system through a growth chamber exhaust gas line consisting of 5 cold traps, a turbo molecular pump 6150, and a tally pump 62.

また、反応室3には準備室4が付設され、この/$備室
4にもターボ分子ポンプ63とロータリーポンプ64か
らなる予備室排気ガスラインを有し系外に通じている。
Further, a preparation chamber 4 is attached to the reaction chamber 3, and this preparation chamber 4 also has a preparation chamber exhaust gas line consisting of a turbo molecular pump 63 and a rotary pump 64, which communicates with the outside of the system.

一方、成長室3に原料を供給しない場合には、バルブv
4〜9を閉じ原料ガスの供給を止め、バルブV10〜1
2およびバルブV22〜24を開くことにより、キャリ
アガスのみコールドトラップ52、バルブV21を経て
系外に放出される。
On the other hand, when the raw material is not supplied to the growth chamber 3, the valve v
Close valves 4 to 9 to stop the supply of raw material gas, and close valves V10 to 1.
By opening 2 and valves V22 to 24, only the carrier gas is discharged to the outside of the system via cold trap 52 and valve V21.

[発明が解決しようとする課題] しかながら、コールドトラップ52および配管のクリー
ニング、すなわちコールドトラップ52および配管を1
00〜200℃に加熱してコールドトラップ52および
配管内部に付着した原料および酸素、窒素、窒素化合物
、炭素化合物といった不純物をガス状にして除去する際
に、これを成長室排気ガス系のターボ分子ポンプ61と
ロータリーポンプB2で行なっていたため、未分解原料
が成長室排気ガスラインにトラップされ、長時間滞留し
、成長室3の真空度の低下、不純物逆汚染を引き起こし
ていた。
[Problems to be Solved by the Invention] However, cleaning the cold trap 52 and the piping, that is, cleaning the cold trap 52 and the piping once
When removing impurities such as raw materials and oxygen, nitrogen, nitrogen compounds, and carbon compounds adhering to the cold trap 52 and inside the pipes by heating to 00 to 200°C, the gas is removed by turbo molecules in the growth chamber exhaust gas system. Since the pump 61 and the rotary pump B2 were used, undecomposed raw materials were trapped in the growth chamber exhaust gas line and remained there for a long time, causing a decrease in the degree of vacuum in the growth chamber 3 and back contamination with impurities.

このため、バルブV21を開き、コールドトラップ52
から原料排気ガスラインを設は常圧で排気を行なってい
た。
Therefore, the valve V21 is opened and the cold trap 52 is opened.
A raw material exhaust gas line was installed and exhaust was carried out at normal pressure.

[発明が解決しようとする課題] 原料供給時には、流量制御器11〜13の上流側をそれ
ぞれ0.3〜1.0Kg/cfflの加圧状態におくこ
とにより、流量制御器11〜16で流量制御を行なって
原料を成長室に供給していたが、成長室に原料を供給し
ない時間には、流量制御器(4〜16の下流は、上述の
ように常圧となっている。
[Problems to be Solved by the Invention] When supplying raw materials, the upstream sides of the flow controllers 11 to 13 are pressurized to 0.3 to 1.0 Kg/cffl, so that the flow controllers 11 to 16 control the flow rate. The raw material was supplied to the growth chamber under control, but when the raw material was not supplied to the growth chamber, the pressure downstream of the flow rate controllers (4 to 16) was at normal pressure as described above.

従って、バルブv10〜12を閉め、バルブv7〜9を
開いた際に、流量制御器14〜16の上流の圧力(常圧
)と成長室3の圧力(10−6〜10−’T orr 
)との圧力差は著しく異なり、流量制御器14〜16で
流量制御したとしても、成長室4は異常に圧力が高まり
、原料が過度に流れ込み、第4図のように薄膜成長開始
時にオーバシュートを起こすこととなる。成長室での良
質かつ均質なエピタキシャル薄膜の成長を行なうために
は、一定量の原料供給が必要であるが、上述のように流
量が過度であると成長速度は大きくなるが、薄膜の不均
一成長やダメージの大きい薄膜の成長となり、好ましい
ことではない。そこで、原料ボンベを開け、キャリアガ
スである水素ガスでバブリングを開始後、原料供給ガス
ラインの原料分圧が定常になるまで30分〜2時間を必
要とする。
Therefore, when the valves v10 to 12 are closed and the valves v7 to 9 are opened, the pressure upstream of the flow rate controllers 14 to 16 (normal pressure) and the pressure in the growth chamber 3 (10-6 to 10-' Torr
), and even if the flow rate is controlled by the flow rate controllers 14 to 16, the pressure in the growth chamber 4 will be abnormally high, and the raw material will flow in excessively, resulting in an overshoot at the start of thin film growth as shown in Figure 4. This will cause In order to grow a high-quality and homogeneous epitaxial thin film in a growth chamber, a certain amount of raw material must be supplied, but as mentioned above, if the flow rate is excessive, the growth rate will increase, but the thin film will become non-uniform. This results in the growth of a thin film with significant growth and damage, which is not desirable. Therefore, after opening the raw material cylinder and starting bubbling with hydrogen gas, which is a carrier gas, it takes 30 minutes to 2 hours until the raw material partial pressure in the raw material supply gas line becomes steady.

また、上述のように、原料を供給しない時間は、原料供
給ガスラインや原料排気ガスラインは常圧なので、ガス
流量が遅く、成長終了後の各ガスラインからの原料の抜
き取りに時間を要したり、原料が各ガスラインの配管に
付着するという課題も有する。また、上述したベーキン
グの際にもかなりの時間を要した。
In addition, as mentioned above, during the time when raw materials are not supplied, the raw material supply gas lines and raw material exhaust gas lines are at normal pressure, so the gas flow rate is slow, and it takes time to extract the raw materials from each gas line after growth is completed. There is also the problem that raw materials adhere to the piping of each gas line. Further, the baking described above also required a considerable amount of time.

このため、バイパスラインである原料排気ガスラインを
コールドトラップ52から、バルブV20を開いてロー
タリーポンプG2に導入することも考えられるが、成長
室3の真空度の低下、不純物逆汚染等の上記課題は何ら
解消されるものではなかった。
For this reason, it is conceivable to introduce the raw material exhaust gas line, which is a bypass line, from the cold trap 52 to the rotary pump G2 by opening the valve V20, but this will cause the above-mentioned problems such as a decrease in the degree of vacuum in the growth chamber 3 and back contamination with impurities. was not resolved in any way.

本発明は、かかる従来技術の課題を解消すべくなされた
もので、薄膜成長開始時に生じるオーバシュートを解消
すると共に、薄膜成長や原料の抜き取り、ベーキングを
短時間で行なえ、かつ原料の配管への付着を防止し得る
気相分子線エピタキシー(気相MBE)装置を提供する
ことを目的とする。
The present invention has been made in order to solve the problems of the prior art, and it eliminates the overshoot that occurs at the start of thin film growth, allows thin film growth, raw material extraction, and baking to be performed in a short time, and also allows the raw material to be connected to piping. It is an object of the present invention to provide a vapor phase molecular beam epitaxy (vapor phase MBE) apparatus that can prevent adhesion.

[課題を解決するための手段] 本発明の上記目的は、原料排気ガスラインのコールドト
ラップ下流に、成長室排気ガスラインに設けられた吸引
ポンプと別個に吸引ポンプを設けることによって達成さ
れる。
[Means for Solving the Problems] The above object of the present invention is achieved by providing a suction pump downstream of the cold trap in the raw material exhaust gas line, separately from the suction pump provided in the growth chamber exhaust gas line.

すなわち、本発明の気相MBE装置は、原料の少なくと
も一部に気相材料を用い、成長室で無機薄膜を成長させ
る気相分子線エピタキシー装置において、原料供給ガス
ラインから系外に通じるバイパスラインである原料排気
ガスラインのコールドトラップ下流に成長室排気ガスラ
インに設けられた吸引ポンプと別個に吸引ポンプを設け
たことを特徴とする。
That is, the vapor phase MBE apparatus of the present invention is a vapor phase molecular beam epitaxy apparatus that uses a vapor phase material as at least a part of the raw material and grows an inorganic thin film in a growth chamber. The present invention is characterized in that a suction pump is provided downstream of the cold trap in the raw material exhaust gas line, separately from the suction pump provided in the growth chamber exhaust gas line.

以下、本発明を図面に基づいて説明する。Hereinafter, the present invention will be explained based on the drawings.

第1図は、本発明の気相MBE装置の一例であるMOM
BE装置の概略図である。同図においては、原料排気ガ
スラインのコールドトラップ52の下流には、メカニカ
ルブースターポンプ65とロータリーポンプ66からな
る吸引ポンプが設けられている。このように2つのポン
プを用いるのはζ得られる薄膜の種類によって成長室3
における成長圧力が異なり、2つのポンプを組合わせて
用いることによって、原料供給ラインの圧力を所望に制
御できるからである。このように、原料排気ガスライン
に新たに吸引ポンプを配置することによって、原料ガス
供給ラインは、原料ガス排気中でもlo−3〜10 ’
 T orrに維持され、各配管のガス流量を 1−1
0cc/ minとすることができる。従って、バルブ
VIO〜12を閉め、バルブv7〜9を開き、薄膜成長
開始時にオバーシュートは起きず、第2図に示されるよ
うに直ちに圧力が定常状態となり、これに伴なって原料
ガス流量も一定となる。
FIG. 1 shows a MOM which is an example of the gas phase MBE apparatus of the present invention.
FIG. 2 is a schematic diagram of a BE device. In the figure, a suction pump consisting of a mechanical booster pump 65 and a rotary pump 66 is provided downstream of the cold trap 52 in the raw material exhaust gas line. The use of two pumps in this way depends on the type of thin film to be obtained in the growth chamber 3.
This is because the growth pressures in the two pumps are different, and by using the two pumps in combination, the pressure in the raw material supply line can be controlled as desired. In this way, by newly arranging a suction pump in the raw material exhaust gas line, the raw material gas supply line can be maintained at lo-3 to 10' even when the raw material gas is exhausted.
The gas flow rate of each pipe is maintained at 1-1 Torr.
It can be set to 0cc/min. Therefore, when valves VIO to VIO12 are closed and valves V7 to V9 are opened, no overshoot occurs when thin film growth starts, and the pressure immediately becomes steady as shown in FIG. 2. Along with this, the raw material gas flow rate also increases. It becomes constant.

また、本発明の装置では、第3図に示されるような流量
制御器14〜18は必要がなく、しかも一定量の原料ガ
スの供給が可能となる。
Further, in the apparatus of the present invention, the flow rate controllers 14 to 18 as shown in FIG. 3 are not necessary, and a constant amount of raw material gas can be supplied.

なお、成長室排気ガスラインを2ライン以上とし、各々
に吸引ポンプを設置し、その1つのラインで成長室から
の排気ガスを導入し、他のラインでコールドトラップか
らの原料排気ガスを導入する態様も本発明に包含される
In addition, there are two or more growth chamber exhaust gas lines, each with a suction pump, and one line introduces the exhaust gas from the growth chamber, and the other line introduces the raw material exhaust gas from the cold trap. Embodiments are also encompassed by the invention.

また、本発明は気相MBE装置を対象とするものである
が、気相材料を原料とする減圧MOCVD装置にも適用
可能である。
Further, although the present invention is directed to a gas-phase MBE apparatus, it is also applicable to a low-pressure MOCVD apparatus using a gas-phase material as a raw material.

[作用・効果コ 以上のような本発明によって、次のような作用・効果を
奏する。
[Operations and Effects] The present invention as described above provides the following operations and effects.

(1)薄膜成長開始時に圧力が直ちに定常状態となり、
これに伴なって原料ガス流量も一定となり、オバーシュ
ートが生じないため、良質かつ均質なエピタキシャル薄
膜が得られる。
(1) At the start of thin film growth, the pressure immediately reaches a steady state,
Along with this, the raw material gas flow rate also becomes constant and overshoot does not occur, so that a high quality and homogeneous epitaxial thin film can be obtained.

(2)原料供給ラインや原料排気ラインが減圧状態で維
持されているので、 a)キャリアガスである水素ガスに対する原料分圧を大
きくできるため、原料供給量を増加できる; b)成長終了後の原料を配管から抜き取るのが短時間で
行なえる; C〉原料ガスの流速が早くなるため、配管への原料ガス
の付着が少ない; d)ベーキングが容易に行なえるので、ベーキング効率
が向上する; (3)原料供給ラインおよび原料排気ラインのベーキン
グを成長室排気ガスラインのポンプを用いないで行なう
ことができるので、成長室の真空度の低下、不純物逆汚
染が起こらない。
(2) Since the raw material supply line and the raw material exhaust line are maintained in a reduced pressure state, a) the partial pressure of the raw material with respect to hydrogen gas, which is the carrier gas, can be increased, so the amount of raw material supplied can be increased; b) after the growth is completed The raw material can be removed from the piping in a short time; C) The flow rate of the raw material gas is faster, so less of the raw material gas adheres to the piping; d) Baking can be performed easily, so baking efficiency is improved; (3) Baking of the raw material supply line and the raw material exhaust line can be carried out without using a pump in the growth chamber exhaust gas line, so that a decrease in the degree of vacuum in the growth chamber and impurity back contamination do not occur.

[実施例] 以下、実施例および比較例に基づいて本発明を具体的に
説明する。
[Examples] The present invention will be specifically described below based on Examples and Comparative Examples.

第1図に示されるMOMBE装置を用い、トリメチルガ
リウムとアルシンを原料とし、G a A S基板ウェ
ハーの上に、エピタキシャルGa As薄膜を成長させ
た(実施例1)。
Using the MOMBE apparatus shown in FIG. 1, an epitaxial GaAs thin film was grown on a GaAs substrate wafer using trimethylgallium and arsine as raw materials (Example 1).

このエピタキシャルGa As薄膜の顕微鏡写真(x 
1000)を第5図に示す。
A micrograph of this epitaxial GaAs thin film (x
1000) is shown in FIG.

また、比較として、第3図に示されるMOMBE装置を
用い、トリメチルガリウムとアルシンを原料とし、Ga
 As基板ウェハーの上に、エピタキシャルGa As
薄膜を成長させた(比較例1)。
In addition, for comparison, using the MOMBE apparatus shown in Figure 3, we used trimethylgallium and arsine as raw materials, and Ga
On top of the As substrate wafer, epitaxial GaAs
A thin film was grown (Comparative Example 1).

このエピタキシャルGa As薄膜の顕微鏡写真(X 
1000)を第6図に示す。
A micrograph of this epitaxial GaAs thin film (X
1000) is shown in FIG.

この第5図と第6図の比較から明らかなように、共通す
るレンズの汚れ等は別として、第5図は表面に凹凸がな
くフラットなのに対し、第6図は単結晶が成長せず、ガ
リウムのドロップレットが生じた。
As is clear from the comparison between Fig. 5 and Fig. 6, apart from the common dirt on the lens, the surface in Fig. 5 is flat with no irregularities, whereas in Fig. 6, no single crystal has grown. Gallium droplets were formed.

また、第1図および第3図の装置を使用後、原料供給ラ
インの配管の汚染度を四重極質量分析によって評価した
ところ、第1図の装置のH20/H2は3.IX 10
−’であったのに対し、第3図の装置ノH20/H2ハ
2.2xlO−3となッテおり、第1図の装置のほうが
約1/7も汚染が低減されていた。なお、CO2や02
等の不純物についても同様の傾向が認められた。
Furthermore, after using the apparatus shown in FIGS. 1 and 3, the degree of contamination of the piping of the raw material supply line was evaluated by quadrupole mass spectrometry, and the H20/H2 of the apparatus shown in FIG. 1 was 3. IX 10
-', whereas the H20/H2 ratio of the apparatus shown in FIG. 3 was 2.2xlO-3, meaning that the apparatus shown in FIG. 1 reduced contamination by about 1/7. In addition, CO2 and 02
A similar tendency was observed for other impurities.

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

第1図は、本発明の気相MBE装置の一例であるMOM
BE装置の概略図、 第2図は、第1図のMOMBE装置を用いて、薄膜成長
を開始させた時の圧力と時間との関係を示すグラフ、 第3図は、従来のMOMBE装置の概略図、第4図は、
第3図のMOMBE装置を用いて、薄膜成長を開始させ
た時の圧力と時間との関係を示すグラフ、 第5図は、実施例1によって得られたエピタキシャルG
a As薄膜の顕微鏡写真(X 1000) 、そして
、 第6図は、比較例1によって得られたエピタキシャルG
a As薄膜の顕微鏡写真(X 1000)。 51、52:コールドトラップ 61〜66:吸引ポンプ
FIG. 1 shows a MOM which is an example of the gas phase MBE apparatus of the present invention.
A schematic diagram of a BE apparatus. Figure 2 is a graph showing the relationship between pressure and time when thin film growth is started using the MOMBE apparatus of Figure 1. Figure 3 is a schematic diagram of a conventional MOMBE apparatus. Figure 4 is
FIG. 3 is a graph showing the relationship between pressure and time when thin film growth is started using the MOMBE apparatus. FIG.
a Micrograph (X 1000) of the As thin film, and Figure 6 shows the epitaxial G obtained in Comparative Example 1.
a Micrograph of As thin film (X 1000). 51, 52: Cold trap 61-66: Suction pump

Claims (1)

【特許請求の範囲】[Claims] 1、原料の少なくとも一部に気相材料を用い、成長室で
無機薄膜を成長させる気相分子線エピタキシー装置にお
いて、原料供給ガスラインから系外に通じるバイパスラ
インである原料排気ガスラインのコールドトラップ下流
に、成長室排気ガスラインに設けられた吸引ポンプと別
個に吸引ポンプを設けたことを特徴とする気相分子線エ
ピタキシー装置。
1. In a vapor phase molecular beam epitaxy apparatus that uses a gas phase material as at least a part of the raw material and grows an inorganic thin film in a growth chamber, a cold trap in the raw material exhaust gas line, which is a bypass line leading from the raw material supply gas line to the outside of the system. A vapor phase molecular beam epitaxy apparatus characterized in that a suction pump is provided downstream, separately from a suction pump provided in a growth chamber exhaust gas line.
JP33824589A 1989-12-28 1989-12-28 Vapor phase molecular beam epitaxy device Pending JPH03201426A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33824589A JPH03201426A (en) 1989-12-28 1989-12-28 Vapor phase molecular beam epitaxy device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33824589A JPH03201426A (en) 1989-12-28 1989-12-28 Vapor phase molecular beam epitaxy device

Publications (1)

Publication Number Publication Date
JPH03201426A true JPH03201426A (en) 1991-09-03

Family

ID=18316294

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33824589A Pending JPH03201426A (en) 1989-12-28 1989-12-28 Vapor phase molecular beam epitaxy device

Country Status (1)

Country Link
JP (1) JPH03201426A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0806499A1 (en) * 1996-05-09 1997-11-12 Sharp Kabushiki Kaisha Method and apparatus for fabricating semiconductor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0806499A1 (en) * 1996-05-09 1997-11-12 Sharp Kabushiki Kaisha Method and apparatus for fabricating semiconductor
US6206969B1 (en) 1996-05-09 2001-03-27 Sharp Kabushiki Kaisha Method and apparatus for fabricating semiconductor

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