JPH0471993B2 - - Google Patents
Info
- Publication number
- JPH0471993B2 JPH0471993B2 JP15613387A JP15613387A JPH0471993B2 JP H0471993 B2 JPH0471993 B2 JP H0471993B2 JP 15613387 A JP15613387 A JP 15613387A JP 15613387 A JP15613387 A JP 15613387A JP H0471993 B2 JPH0471993 B2 JP H0471993B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- flow path
- gas flow
- raw material
- valve
- 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.)
- Expired
Links
- 239000007789 gas Substances 0.000 claims description 100
- 239000002994 raw material Substances 0.000 claims description 35
- 238000001947 vapour-phase growth Methods 0.000 claims description 16
- 238000010926 purge Methods 0.000 claims description 14
- 239000012159 carrier gas Substances 0.000 claims description 7
- 230000014759 maintenance of location Effects 0.000 description 7
- 229910001218 Gallium arsenide Inorganic materials 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 125000002524 organometallic group Chemical group 0.000 description 4
- 239000012535 impurity Substances 0.000 description 3
- 239000004065 semiconductor Substances 0.000 description 3
- 229910000980 Aluminium gallium arsenide Inorganic materials 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000000927 vapour-phase epitaxy Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000004678 hydrides Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 150000002902 organometallic compounds Chemical class 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
Landscapes
- Crystals, And After-Treatments Of Crystals (AREA)
- Chemical Vapour Deposition (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は半導体層を再現性よくエピタキシヤル
成長させ、かつ急峻な組成変化、不純物分布を形
成させることのできる気相成長用バルブに関する
ものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a vapor phase growth valve that can epitaxially grow a semiconductor layer with good reproducibility and can form a steep compositional change and impurity distribution. be.
従来、化合物半導体の気相成長、特に有機金属
化合物および水素化物を原料として用いる熱分解
気相成長(以下、有機金属気相成長)における原
料ガスの切換えは、例えば第2図に示すような3
方向バルブを用いて行われるものが一般的であ
る。以下、第2図を参照して従来技術を説明す
る。
Conventionally, switching of source gas in vapor phase growth of compound semiconductors, particularly in pyrolytic vapor phase growth (hereinafter referred to as organometallic vapor phase epitaxy) using organometallic compounds and hydrides as raw materials, has been carried out using, for example, three steps as shown in Fig. 2.
This is generally done using a directional valve. The prior art will be explained below with reference to FIG.
第2図は一般的に有機金属気相成長において用
いられる原料ガス切換えのための3方向バルブを
示す図で、同図イは原料ガス供給状態を示す図、
同図ロは原料ガス排出状態を示す図である。図中
1は原料ガス導入口、2は反応炉への供給ライ
ン、3は排出ライン、4はガス流路を切換えるた
めのシリンダ、5は原料ガス流路、6はバルブ内
の原料ガス滞留領域、7は駆動源を示している。 Fig. 2 is a diagram showing a three-way valve for switching the source gas commonly used in organometallic vapor phase epitaxy;
FIG. 4B is a diagram showing the raw material gas discharge state. In the figure, 1 is the raw material gas inlet, 2 is the supply line to the reactor, 3 is the discharge line, 4 is the cylinder for switching the gas flow path, 5 is the raw material gas flow path, and 6 is the raw material gas retention area in the valve. , 7 indicates a driving source.
図において、原料ガスを切換える場合には、例
えば空気圧源、電磁石等の駆動源7により空気
圧、あるいは電磁的な操作によりシリンダ4を移
動させ、原料ガス流路5を供給ライン2から排出
ライン3へあるいは排出ライン3から供給ライン
2へ切換えることにより行われる。この場合の原
料ガス流路は第2図イの斜線部分5から第2図ロ
の斜線部分5のように変化する。 In the figure, when switching the raw material gas, the cylinder 4 is moved by pneumatic or electromagnetic operation using a drive source 7 such as a pneumatic pressure source or an electromagnet, and the raw material gas flow path 5 is moved from the supply line 2 to the discharge line 3. Alternatively, this can be done by switching from the discharge line 3 to the supply line 2. In this case, the raw material gas flow path changes from the shaded area 5 in FIG. 2A to the shaded area 5 in FIG. 2B.
しかしながら、このような3方向バルブを用い
た原料ガスの切換えにおいては、第2図ロの原料
ガス滞留領域6の部分が必然的に存在し、この滞
留した原料ガスの拡散が原因となり、エピタキシ
ヤル層の特性の再現性およびヘテロ界面の急峻性
などを著しく低下させていた。
However, in switching the raw material gas using such a three-way valve, the raw material gas retention area 6 shown in FIG. The reproducibility of the layer properties and the steepness of the heterointerface were significantly reduced.
さらに原料ガスの切換えにより供給ラインのガ
ス流量が変化するため成長条件が変化し、エピタ
キシヤル層の特性が変化するという問題も生じて
いた。 Furthermore, changing the raw material gas changes the gas flow rate in the supply line, resulting in changes in growth conditions and a problem in that the characteristics of the epitaxial layer change.
また、このような3方向バルブを集合化し、第
2図ロの滞留領域を極めて小さな容積とする気相
成長用マニホールドが知られているが、原理的に
原料ガスの滞留領域はある有限の値を有し、ま
た、供給ラインのガス流量変化も存在するために
上記の問題を根本的に解決するに至つていない。 In addition, a manifold for vapor phase growth is known in which such three-way valves are aggregated and the retention area shown in Figure 2 (b) has an extremely small volume, but in principle, the retention area of the raw material gas is limited to a certain finite value. Furthermore, since there is also a change in the gas flow rate in the supply line, the above problem has not been fundamentally solved.
本発明は、上記の問題点を解決するために、切
換えバルブ内に原料ガスの滞留領域が存在せず、
かつ供給ラインのガス流量が変化しない構造とす
ることにより高品質な半導体層を再現性よくエピ
タキシヤル成長させ、かつ急峻な組成変化、不純
分布を形成させることを可能とする気相成長用バ
ルブを提供することを目的とする。 In order to solve the above-mentioned problems, the present invention eliminates the retention area of raw material gas in the switching valve,
In addition, by creating a structure in which the gas flow rate of the supply line does not change, we have developed a vapor phase growth valve that enables epitaxial growth of high-quality semiconductor layers with good reproducibility, as well as the formation of steep compositional changes and impurity distributions. The purpose is to provide.
そのために本発明の気相成長バルブは、気相成
長装置に用いる原料ガス切換えバルブにおいて、
原料ガス導入口、パージ用ガス導入口、反応炉ガ
ス供給口、およびガス排出口を有する環状に配置
されたガス流路と、該ガス流路内に配置され、原
料ガス導入口から反応炉ガス供給口への第1のガ
ス流路と、パージ用ガス導入口から反応炉ガス供
給口への第2のガス流路とを切り換える第1のガ
ス流路切り換え手段と、原料ガス導入口からガス
排出口への第3のガス流路と、パージ用ガス導入
口からガス排出口への第4のガス流路とを切り換
える第2のガス流路切り換え手段と、第1のガス
流路と第4のガス流路、第2のガス流路と第3の
ガス流路がそれぞれ同時に開閉するように第1,
第2のガス流路切り換え手段を駆動する駆動手段
とを備えたことを特徴とする。
For this purpose, the vapor growth valve of the present invention has the following features in the source gas switching valve used in the vapor growth apparatus:
A gas channel arranged in an annular shape having a raw material gas inlet, a purge gas inlet, a reactor gas supply port, and a gas discharge port; a first gas flow path switching means for switching between a first gas flow path to the supply port and a second gas flow path from the purge gas inlet to the reactor gas supply port; a second gas flow path switching means for switching between a third gas flow path to the exhaust port and a fourth gas flow path from the purge gas inlet to the gas discharge port; The first gas flow path, the second gas flow path and the third gas flow path are opened and closed at the same time, respectively.
and a driving means for driving the second gas flow path switching means.
本発明の気相成長用バルブは、ガス流路を環状
に配置して各ガス導入口より原料ガスとパージ用
ガスとを流入させてガス流路切り換え手段により
ガス流路を切り換えることにより、ガス流路変更
時にバルブ内の反応炉への供給ラインに原料ガス
の滞留領域が存在せず、かつ反応炉への供給ライ
ンの全ガス流量が変化しないようにして急峻な原
料ガスの切り換えを達成することができる。
The vapor phase growth valve of the present invention arranges the gas flow paths in an annular shape, allows the raw material gas and the purge gas to flow in from each gas inlet, and switches the gas flow paths using the gas flow path switching means. When changing the flow path, there is no stagnation area of the raw material gas in the supply line to the reactor inside the valve, and the total gas flow rate in the supply line to the reactor does not change, thereby achieving a sharp switching of the raw material gas. be able to.
以下、実施例を図面を参照して説明する。 Examples will be described below with reference to the drawings.
第1図は本発明による気相成長用バルブの実施
例を示す図であり、同図イは原料ガス供給状態を
示す図、同図ロは原料ガス排出状態を示す図であ
る。図中、第1図で示したものと同一内容のもの
は同一番号で示している。なお、4a,4bはシ
リンダ、7a,7bは駆動源、8はパージ用キヤ
リヤガスの導入口である。 FIG. 1 is a diagram showing an embodiment of a valve for vapor phase growth according to the present invention, in which FIG. 1A shows a raw material gas supply state, and FIG. 1B shows a raw material gas discharge state. In the figure, parts that are the same as those shown in FIG. 1 are designated by the same numbers. Note that 4a and 4b are cylinders, 7a and 7b are drive sources, and 8 is an inlet for a carrier gas for purging.
図において、ガス流路は環状に配置され、各流
路にシリンダ4a,4bが配置されてそれぞれ駆
動源7a,7bにより駆動されるように構成され
ている。 In the figure, the gas flow paths are arranged in an annular shape, and cylinders 4a and 4b are arranged in each flow path and are configured to be driven by drive sources 7a and 7b, respectively.
まず、原料ガスを供給する場合には、駆動源7
a,7bを動作させてシリンダ4a,4bを第1
図イに示す位置に駆動し、原料ガス供給口1より
流入した原料ガスは供給ライン2を通つて反応炉
へ流入し、この時、原料ガスと同流量のパージ用
キヤリヤガスが導入口8より流入し、排出ライン
3を通つて排出されている。 First, when supplying raw material gas, drive source 7
a, 7b to move the cylinders 4a, 4b to the first position.
Driven to the position shown in Figure A, the raw material gas flowing in from the raw material gas supply port 1 flows into the reactor through the supply line 2, and at this time, a purge carrier gas of the same flow rate as the raw material gas flows in from the inlet 8. and is discharged through the discharge line 3.
次に、原料ガス排出の場合には、駆動源7a,
7bによりシリンダ4a,4bを第1図ロの位置
に駆動する。この場合は、導入口1より流入した
原料ガスが排出ライン3を通つて排出されてい
る。この時、原料ガスと同流量のパージ用キヤリ
ヤガスは導入口7より流入し供給ライン2を通つ
て反応炉へ流入する。 Next, in the case of raw material gas discharge, the driving source 7a,
7b drives the cylinders 4a and 4b to the position shown in FIG. 1B. In this case, the raw material gas that has flowed in from the inlet 1 is discharged through the discharge line 3. At this time, the purge carrier gas having the same flow rate as the raw material gas flows from the inlet 7 and flows into the reactor through the supply line 2.
このようにガス流路を環状に配置し、2つのシ
リンダを同時に駆動させ、パージ用キヤリヤガス
の流入によりバルブ内に存在している原料ガスは
すべてパージされるので、バルブ内の原料ガスの
滞留領域は残存しない構造となる。また、原料ガ
スとパージ用キヤリヤガスは同流量に設定されて
いるので、反応炉へ流入する全ガス流量は原料ガ
スの切換えにより変化することはない。さらに、
各原料ガスについて切り換えバルブの供給ライン
および排出ラインをそれぞれ共通にすることがで
きるので、集合化し小型化することも可能であ
る。 In this way, by arranging the gas flow path in an annular shape and driving the two cylinders simultaneously, all the raw material gas existing in the valve is purged by the inflow of the purge carrier gas, so the raw material gas retention area in the valve is becomes a structure that will not survive. Further, since the raw material gas and the purge carrier gas are set at the same flow rate, the total gas flow rate flowing into the reactor does not change due to switching of the raw material gas. moreover,
Since the supply line and the discharge line of the switching valve can be made common for each source gas, it is also possible to aggregate them and downsize them.
以上説明した本発明による気相成長用バルブを
備えた有機金属気相成長装置を用いてアンドープ
GaAsを成長させたところ、n型で残存キヤリヤ
濃度1014〜1015cm-3のエピタキシヤル層が再現性
良く得られ、また、P型不純物ドーピングを行つ
た直後のアンドープGaAsエピタキシヤル層にお
いても、残存キヤリヤ濃度1014〜1015cm-3のn型
を示し、高品質なエピタキシヤル層が再現性良く
得られることが確認された。
Undoping is performed using the organometallic vapor phase growth apparatus equipped with the vapor phase growth valve according to the present invention as described above.
When GaAs was grown, an n-type epitaxial layer with a residual carrier concentration of 10 14 to 10 15 cm -3 was obtained with good reproducibility, and even in an undoped GaAs epitaxial layer immediately after doping with P-type impurities. , the residual carrier concentration was n-type with a residual carrier concentration of 10 14 to 10 15 cm -3 , and it was confirmed that a high quality epitaxial layer could be obtained with good reproducibility.
また、GaAsとAl0.5Ga0.5Asのヘテロ構造をエ
ピタキシヤル成長させ、組成変化の急峻性を測定
した結果、両者の遷移領域は1〜2原子層(<5
Å)と見積られ、非常に急峻な界面を形成するこ
とが確認された。 In addition, as a result of epitaxially growing a heterostructure of GaAs and Al 0.5 Ga 0.5 As and measuring the steepness of the composition change, it was found that the transition region of both is 1 to 2 atomic layers (<5
Å), and it was confirmed that a very steep interface was formed.
なお、上記実施例ではGaAs,AlGaAsの有機
金属気相成長を例に説明したが、本発明は
GaAs,AlGaAsに限定されるものでなく、また、
反応炉の形状、圧力等にも一切限定されず、全て
の単結晶、多結晶、非晶質、金属の気相成長に適
用できることは勿論である。 Note that although the above embodiments have been explained using organometallic vapor phase growth of GaAs and AlGaAs as examples, the present invention
It is not limited to GaAs, AlGaAs, and
It goes without saying that the method is not limited to the shape or pressure of the reactor, and can be applied to all types of single crystal, polycrystal, amorphous, and metal vapor phase growth.
第1図は本発明による気相成長用バルブの実施
例を示す図、第2図は従来の有機金属気相成長に
用いられる原料ガス切換えのため3方向バルブを
示す図である。
1…原料ガス導入口、2…供給ライン、3…排
出ライン、4,4a,4b…シリンダ、5…原料
ガス流路、6…原料ガス滞留領域、7,7a,7
b…駆動源、8…パージ用キヤリヤガス導入口。
FIG. 1 is a diagram showing an embodiment of a valve for vapor phase growth according to the present invention, and FIG. 2 is a diagram showing a three-way valve for switching source gases used in conventional metal organic vapor phase growth. DESCRIPTION OF SYMBOLS 1... Raw material gas inlet, 2... Supply line, 3... Discharge line, 4, 4a, 4b... Cylinder, 5... Raw material gas flow path, 6... Raw material gas retention area, 7, 7a, 7
b...Drive source, 8...Carrier gas inlet for purge.
Claims (1)
において、原料ガス導入口、パージ用ガス導入
口、反応炉ガス供給口、およびガス排出口を有す
る環状に配置されたガス流路と、該ガス流路内に
配置され、原料ガス導入口から反応炉ガス供給口
への第1のガス流路と、パージ用ガス導入口から
反応炉ガス供給口への第2のガス流路とを切り換
える第1のガス流路切換え手段と、原料ガス導入
口からガス排出口への第3のガス流路と、パージ
用ガス導入口からガス排出口への第4のガス流路
とを切り換える第2のガス流路切り換え手段と、
第1のガス流路と第4のガス流路、第2のガス流
路と第3のガス流路がそれぞれ同時に開閉するよ
うに第1,第2のガス流路切り換え手段を駆動す
る駆動手段とを備えた気相成長バルブ。 2 第1,第2のガス流路切り換え手段はシリン
ダからなる特許請求の範囲第1項記載の気相成長
バルブ。 3 前記パージ用キヤリアガスは、原料ガスと同
流量流入させ、ガス流路変更時に反応炉への供給
ラインの全ガス流量が変化しないようにした特許
請求の範囲第1項記載の気相成長用バルブ。 4 前記ガス流路切換え手段、及び環状のガス流
路を単一のブロツクに組み込み、ガス供給ライ
ン、及び排出ラインをそれぞれ共通とし、集合化
した特許請求の範囲第1項記載の気相成長用バル
ブ。[Scope of Claims] 1. In a source gas switching valve used in a vapor phase growth apparatus, a gas flow path arranged in an annular shape having a source gas inlet, a purge gas inlet, a reactor gas supply port, and a gas outlet. and a first gas flow path arranged in the gas flow path from the raw material gas inlet to the reactor gas supply port, and a second gas flow path from the purge gas inlet to the reactor gas supply port. a third gas flow path from the source gas inlet to the gas outlet; and a fourth gas flow path from the purge gas inlet to the gas outlet. a second gas flow path switching means for switching;
Driving means for driving the first and second gas passage switching means so that the first gas passage and the fourth gas passage, and the second gas passage and the third gas passage are opened and closed simultaneously, respectively. Vapor growth valve with. 2. The vapor growth valve according to claim 1, wherein the first and second gas flow path switching means comprises a cylinder. 3. The vapor phase growth valve according to claim 1, wherein the purge carrier gas is allowed to flow in the same flow rate as the raw material gas, so that the total gas flow rate in the supply line to the reactor does not change when changing the gas flow path. . 4. For vapor phase growth according to claim 1, in which the gas flow path switching means and the annular gas flow path are incorporated into a single block, and the gas supply line and the discharge line are common, respectively, and are aggregated. valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15613387A JPS64268A (en) | 1987-06-23 | 1987-06-23 | Valve for vapor growth |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15613387A JPS64268A (en) | 1987-06-23 | 1987-06-23 | Valve for vapor growth |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| JPH01268A JPH01268A (en) | 1989-01-05 |
| JPS64268A JPS64268A (en) | 1989-01-05 |
| JPH0471993B2 true JPH0471993B2 (en) | 1992-11-17 |
Family
ID=15621044
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15613387A Granted JPS64268A (en) | 1987-06-23 | 1987-06-23 | Valve for vapor growth |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS64268A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1486707B1 (en) * | 2003-06-11 | 2007-11-21 | Asm International N.V. | Gas supply system, valve assembly and method of forming reactant pulses by operating a valve assembly |
-
1987
- 1987-06-23 JP JP15613387A patent/JPS64268A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS64268A (en) | 1989-01-05 |
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