JPH04337627A - Vapor growth device - Google Patents

Vapor growth device

Info

Publication number
JPH04337627A
JPH04337627A JP10946591A JP10946591A JPH04337627A JP H04337627 A JPH04337627 A JP H04337627A JP 10946591 A JP10946591 A JP 10946591A JP 10946591 A JP10946591 A JP 10946591A JP H04337627 A JPH04337627 A JP H04337627A
Authority
JP
Japan
Prior art keywords
gas
growth
substrate
grown
raw material
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
JP10946591A
Other languages
Japanese (ja)
Inventor
Koichi Kaneda
金田 幸一
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.)
Fujitsu Ltd
Original Assignee
Fujitsu 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 Fujitsu Ltd filed Critical Fujitsu Ltd
Priority to JP10946591A priority Critical patent/JPH04337627A/en
Publication of JPH04337627A publication Critical patent/JPH04337627A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide a vapor growth device which can grow an epitaxial growth layer with a uniform thickness regardless of size differences in the growth substrate, not require the replacement of growth tools such as the reaction tube and the gas jet nozzle, and effectively use the source as without jetting an excessive amount of source gas for vertical vapor growth devices, especially MOVPE devices. CONSTITUTION:This device is designed with multiple gas spray outlets 51-5n which introduce the gas from one direction into the reation container and in the vapor growth device in which these gas jet outlets 51-5n are placed opposite a growth substrate 4, with a capability to independently switch the gas introduced to the reaction container through each individual gas spray outlet 51-5n between a 1st gas 1 which contains the growth material and a 2nd gas 2 which does not contain the growth material.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は気相成長装置、特に光通
信用の発光、受光素子等を製造するための化合物半導体
エピタキシャルウエーハを製造する際に用いるMOVP
E(有機金属気相エピタキシャル)装置等の縦型の気相
成長装置に関する。
[Industrial Application Field] The present invention relates to a vapor phase growth apparatus, particularly an MOVP used in manufacturing compound semiconductor epitaxial wafers for manufacturing light emitting and light receiving elements for optical communications.
The present invention relates to a vertical vapor phase growth apparatus such as an E (organic metal vapor phase epitaxial) apparatus.

【0002】エピタキシャルウエーハの製造では、大面
積にわたって均一な成長膜厚が得られることが望まれる
。そのため均一な成長膜厚を得る一方法として、近時、
縦型のMOVPE装置を用い、且つ複数のノズルから成
長原料を含むガス(成長ガス)を被成長基板面に向かっ
て吹出させるようにすることによって、ガスの対流や滞
留によるガス流の乱れを抑えて被成長基板上で成長ガス
の層流を実現し、これによって成長膜厚の均一性を高め
る方法が提案されている。
In the production of epitaxial wafers, it is desired to obtain a uniform growth film thickness over a large area. Therefore, as a method to obtain a uniform grown film thickness, recently,
By using a vertical MOVPE device and blowing out the gas containing the growth material (growth gas) toward the growth substrate surface from multiple nozzles, disturbances in the gas flow due to gas convection and stagnation can be suppressed. A method has been proposed in which a laminar flow of the growth gas is realized on the growth substrate, thereby improving the uniformity of the grown film thickness.

【0003】しかしこの方法は、一定の寸法形状を有す
る被成長基板に対しては十分な効果が得られるが、光素
子用のエピタキシャルウエーハの製造に用いる被成長基
板のように、基板の寸法、形状が、円形、矩形、大面積
、小面積等種々に異なる場合には、成長ガスの消費効率
の低下、欠陥の発生等の面で不十分であり、改良が望ま
れていた。
However, although this method is sufficiently effective for growth substrates having fixed dimensions and shapes, there are cases where the dimensions of the substrate, such as the growth substrates used in the production of epitaxial wafers for optical devices, vary. When the shapes are different, such as circular, rectangular, large area, small area, etc., the growth gas consumption efficiency is lowered, defects occur, etc., and improvements are desired.

【0004】0004

【従来の技術】図3は従来の縦型MOVPE装置の縦方
向断面模式図で、図中、1は成長原料を含んだガスの供
給管、3はカーボンサセプタ、3Pは基板搭載溝、4は
被成長基板、51 、52 、53 、54 、55 
はガス吹き出しノズル、61 、62 、63 、64
 、65 はガス流量制御手段、71 、72 、73
 、74 、75 はストップパルブ、11は真空排気
口、12は反応容器(反応管)、13はサセプタを定速
で回転させる回転軸を示す。
[Prior Art] Fig. 3 is a schematic longitudinal cross-sectional view of a conventional vertical MOVPE apparatus, in which 1 is a gas supply pipe containing growth raw materials, 3 is a carbon susceptor, 3P is a substrate mounting groove, and 4 is a Growth substrate, 51 , 52 , 53 , 54 , 55
are gas blowing nozzles, 61 , 62 , 63 , 64
, 65 is a gas flow rate control means, 71 , 72 , 73
, 74 and 75 are stop valves, 11 is a vacuum exhaust port, 12 is a reaction vessel (reaction tube), and 13 is a rotation shaft for rotating the susceptor at a constant speed.

【0005】同装置を用いた従来のエピタキシャル成長
においては、サセプタ3に形成されている基板搭載溝3
Pに適合する被成長基板4上の成長膜厚が均一になるよ
うに各々のノズル51 〜55 から吹出す成長原料を
含んだガスの流量を制御し、被成長基板4の大小に係わ
らず常に同一条件で総てのノズル51 〜55 から成
長原料を含んだガスを吹出させることにより、ガスの対
流や滞留を防止して均一な膜厚のエピタキシャル成長を
行うか(第1の方法)、若しくは被成長基板毎にその形
状や大きさに見合った反応容器(反応管)及びガス吹出
しノズル等の成長治具に交換することによって成長膜厚
の均一化を図って成長を行う方法(第2の方法)が用い
られていた。
In conventional epitaxial growth using the same device, the substrate mounting groove 3 formed in the susceptor 3
The flow rate of the gas containing the growth material blown out from each nozzle 51 to 55 is controlled so that the thickness of the grown film on the growth substrate 4 that conforms to P is uniform, and the Either the gas containing the growth raw material is blown out from all the nozzles 51 to 55 under the same conditions to prevent gas convection and stagnation and epitaxial growth with a uniform film thickness is performed (first method); A method of growing with a uniform growth film thickness by replacing each growth substrate with a growth jig such as a reaction vessel (reaction tube) and a gas blowing nozzle that match the shape and size of the growth substrate (second method) ) was used.

【0006】[0006]

【発明が解決しようとする課題】従って、前記第1の方
法によれば、小さな基板上に成長を行う際、成長に寄与
しない余分な原料ガスを流すことになって不経済である
と同時に、基板以外の部分(主としてカーボンサセプタ
上)に付着する分解生成物の増加により、この分解生成
物の剥脱飛散粒子に起因する表面欠陥が生じ易くなると
いう問題が生じていた。また、前記第2の方法によれば
、反応管、ノズル等の交換、雰囲気の安定化、条件設定
等の手番のためにスループットが低下するという問題が
あった。
Therefore, according to the first method, when performing growth on a small substrate, an excess raw material gas that does not contribute to growth is flowed, which is uneconomical, and at the same time, The increase in decomposition products adhering to parts other than the substrate (mainly on the carbon susceptor) has caused a problem in that surface defects are likely to occur due to exfoliated and scattered particles of the decomposition products. Further, according to the second method, there is a problem that the throughput is reduced due to steps such as replacing reaction tubes, nozzles, etc., stabilizing the atmosphere, and setting conditions.

【0007】そこで本発明は、被成長基板の大小に係わ
らず均一な膜厚のエピタキシャル成長層を、反応容器(
反応管)、ガス吹出しノズル等の成長治具を交換するこ
となく、また余分な原料ガスを流さず原料ガスを有効に
使って成長することができる気相成長装置を提供するこ
とを目的とする。
Therefore, the present invention aims to grow an epitaxially grown layer of uniform thickness regardless of the size of the substrate to be grown in a reaction vessel (
The purpose of the present invention is to provide a vapor phase growth apparatus that allows growth by effectively using raw material gas without replacing growth jigs such as reaction tubes and gas blowing nozzles, and without flowing excess raw material gas. .

【0008】[0008]

【課題を解決するための手段】上記課題の解決は、反応
容器内へ一方向からガスを導入する複数のガス吹き出し
口を有し、被成長基板が該ガス吹出し口に対向して配置
される気相成長装置において、成長原料を含む第1のガ
スと、成長原料を含まない第2のガスとを、個々のガス
吹出し口について独立に切り換えて反応容器内へ導入す
ることを可能にした本発明による気相成長装置によって
達成される。
[Means for Solving the Problems] A solution to the above problem is to have a plurality of gas outlets for introducing gas from one direction into a reaction vessel, and a substrate to be grown to be grown facing the gas outlets. In a vapor phase growth apparatus, this book enables a first gas containing a growth material and a second gas not containing a growth material to be introduced into a reaction vessel by independently switching each gas outlet. This is achieved by a vapor phase growth apparatus according to the invention.

【0009】[0009]

【作用】図1は本発明の原理説明用模式図で(a) は
ガス吹き出しノズル配置を示す平面図、(b) は装置
要部の縦方向断面模式図である。
FIG. 1 is a schematic diagram for explaining the principle of the present invention, in which (a) is a plan view showing the arrangement of gas blowing nozzles, and (b) is a schematic longitudinal sectional view of the main parts of the device.

【0010】この図に示すように本発明の気相成長装置
においては、例えば上部壁面の同一平面S上に例えば図
(a) のような配置でn個のガス吹出しノズル5が整
列配置され、図(b) に示すように、各々のノズル5
1 〜5n それぞれの手前にガス流量制御手段61 
〜6n が接続され、各ガス流量制御手段61 〜6n
 はそれぞれ第1の配管91 〜9n 及び第1のスト
ップバルブ71 〜7n を経て成長原料を含むガスの
供給管1に接続される。そして更に第1の配管91 〜
9n には、それぞれバイパスとして第2の配管101
 〜10n が接続され、この第2の配管101 〜1
0n はそれぞれ第2のストップバルブ81 〜8n 
を介し成長原料を含まないガスの供給管2に接続されて
構成される。
As shown in this figure, in the vapor phase growth apparatus of the present invention, n gas blowing nozzles 5 are arranged, for example, on the same plane S of the upper wall surface, as shown in figure (a). As shown in Figure (b), each nozzle 5
1 to 5n Gas flow rate control means 61 in front of each
~6n are connected, and each gas flow rate control means 61 ~6n
are connected to the gas supply pipe 1 containing the growth raw material via first pipes 91 to 9n and first stop valves 71 to 7n, respectively. Furthermore, the first pipe 91 ~
9n, each has a second pipe 101 as a bypass.
~10n is connected, and this second piping 101 ~1
0n are second stop valves 81 to 8n, respectively.
It is configured to be connected to a gas supply pipe 2 that does not contain a growth material through a gas supply pipe 2.

【0011】このような構成を有する本発明に係る気相
成長装置においては、このノズル面に対向して配置され
る直径Lの第1の被成長基板4上に成長を行う際には、
第1のストップバルブ71 〜7n を開き、第2のス
トップバルブ81 〜8n を閉じて、総てのガス吹き
出しノズル51 〜5n から成長原料を含むガスを放
出導入することにより直径Lの第1の被成長基板4上に
均一厚さのエピタキシャル層の成長を行う。その後、例
えば前記第1の被成長基板4より小さい直径lの第2の
被成長基板4′上に成長を行う際には、この基板4′上
に対向するガス吹出しノズル例えば53 〜5n−2 
に対応する第1のストップバルブ73 〜7n−2 を
開き、第2のストップバルブ83 〜8n−2 を閉じ
てこれらガス吹出しノズル53 〜5n−2 から成長
原料を含んだガスを導入し、前記第2の被成長基板4′
上から外れた位置のガス吹き出しノズル51 〜52 
及び5n−1 〜5n に対応する第1のストップバル
ブ71 〜72 及び7n−1 〜7n を閉じ、第2
のストップバルブ81 〜82 及び8n−1 〜8n
 を開いてガス吹き出しノズル51 〜52 及び5n
−1 〜5n から成長原料を含まないガス例えば水素
を、第1の被成長基板4の場合にこれらノズルから導入
された原料を含んだガスとほぼ等しい流量で導入し、直
径lの小さい第2の被成長基板4′上に均一な厚さのエ
ピタキシャル層の成長を行う。
In the vapor phase growth apparatus according to the present invention having such a configuration, when performing growth on the first growth target substrate 4 having a diameter L placed opposite to the nozzle surface,
The first stop valves 71 to 7n are opened, the second stop valves 81 to 8n are closed, and the gas containing the growth raw material is released and introduced from all the gas blowing nozzles 51 to 5n. An epitaxial layer with a uniform thickness is grown on the growth substrate 4. Thereafter, for example, when performing growth on a second growth target substrate 4' having a smaller diameter l than the first growth target substrate 4, a gas blowing nozzle, for example 53 to 5n-2, opposite to this substrate 4' is used.
The first stop valves 73 to 7n-2 corresponding to the above are opened, the second stop valves 83 to 8n-2 are closed, and the gas containing the growth raw material is introduced from these gas blowing nozzles 53 to 5n-2. Second growth substrate 4'
Gas blowing nozzles 51 to 52 located off the top
and 5n-1 to 5n, the first stop valves 71 to 72 and 7n-1 to 7n are closed, and the second stop valves are closed.
Stop valves 81 to 82 and 8n-1 to 8n
Open the gas blowing nozzles 51 to 52 and 5n.
-1 to 5n, a gas containing no growth material, such as hydrogen, is introduced at a flow rate approximately equal to that of the gas containing the material introduced from these nozzles in the case of the first growth substrate 4, and An epitaxial layer of uniform thickness is grown on the growth substrate 4'.

【0012】上記成長において、各ガス吹出しノズル5
1 〜5nから放出されるガス流量及び成長原料を含む
ガスの原料濃度は、ほぼ一定とする。従って上記本発明
の気相成長装置によれば被成長基板の大きさにほぼ比例
した成長原料を含むガスを流せばよく、原料ガスの節減
が図れる。
In the above growth, each gas blowing nozzle 5
The gas flow rate discharged from 1 to 5n and the raw material concentration of the gas containing the growth raw material are approximately constant. Therefore, according to the vapor phase growth apparatus of the present invention, it is sufficient to flow a gas containing a growth material approximately proportional to the size of the substrate to be grown, and the amount of material gas can be reduced.

【0013】また、被成長基板が小さい場合にも、被成
長基板の周辺に表出しているサセプタ上に反応生成物が
堆積することがなくなるので、反応生成物の剥脱飛散粒
子による成長欠陥の発生は回避される。
[0013] Furthermore, even when the growth substrate is small, the reaction products are not deposited on the susceptor exposed around the growth substrate, which prevents the occurrence of growth defects due to exfoliated and scattered particles of the reaction products. is avoided.

【0014】[0014]

【実施例】以下本発明を、一実施例について、図2に示
す装置要部の縦方向断面模式図を参照して具体的に説明
する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to a schematic longitudinal sectional view of the main parts of the apparatus shown in FIG.

【0015】この実施例に用いた縦型MOVPE装置は
、底部に真空排気口11を有する反応容器(反応管)1
2の上部の同一平面上に例えば一列に5本のガス吹き出
しノズル51 〜55 が順次配置され、この反応容器
12内に被成長基板4をノズル面に平行に対向して支持
する例えばカーボンからなるサセプタ3が回転軸13に
よって支持されて配置され、前記ガス吹出しノズル51
 〜55 はそれぞれガス流量制御手段61 〜65 
、第1の配管91 〜95 及び第1のストップバルブ
71 〜75 を順次介して成長原料を含むガスの供給
管1に接続され、且つ第1の配管91 〜95 にはそ
れぞれバイパスとして第2の配管101 〜105が接
続され、これら第2の配管101 〜105 がそれぞ
れ第2のストップバルブ81 〜85 を介して成長原
料を含まないガスの供給管2に接続された構造を有する
The vertical MOVPE apparatus used in this example has a reaction vessel (reaction tube) 1 having a vacuum exhaust port 11 at the bottom.
For example, five gas blowing nozzles 51 to 55 are sequentially arranged in a row on the same plane on the upper part of the reaction vessel 12, and the growth substrate 4 is supported in the reaction vessel 12 so as to face parallel to the nozzle surface. A susceptor 3 is disposed supported by a rotation shaft 13, and the gas blowing nozzle 51
~55 are gas flow rate control means 61 ~65, respectively.
, first pipes 91 to 95 and first stop valves 71 to 75 in order to the supply pipe 1 for the gas containing the growth raw material, and each of the first pipes 91 to 95 is connected to a second pipe as a bypass. It has a structure in which pipes 101 to 105 are connected, and these second pipes 101 to 105 are connected to a gas supply pipe 2 that does not contain a growth material via second stop valves 81 to 85, respectively.

【0016】この装置を用い例えばインジウム燐〔In
P〕のエピタキシャル成長を行う際には、原料ガスとし
て20%フォスフィン[PH3] (水素ベース)  
とトリメチルインジウム[(CH3)3In](昇華容
器温度20℃)を用い、20%PH3 1000ccm
 と(CH3)3In150ccmをキャリアガスであ
る水素[H2]8850ccm に混入して成長原料を
含む第1のガスを調整した。また成長原料を含まない第
2のガスにはH2ガスを用いた。
Using this device, for example, indium phosphorus [In
When epitaxially growing P], 20% phosphine [PH3] (hydrogen-based) is used as the raw material gas.
and trimethylindium [(CH3)3In] (sublimation vessel temperature 20°C), 20% PH3 1000 ccm
A first gas containing a growth raw material was prepared by mixing 150 ccm of (CH3)3In with 8850 ccm of hydrogen [H2] as a carrier gas. Moreover, H2 gas was used as the second gas that does not contain the growth material.

【0017】そして、ガス吹き出しノズル51 〜55
 までのの配置寸法に対応する例えば直径3インチの例
えばInPからなる被成長基板4上へのInP層のエピ
タキシャルに際しては、第1のストップバルブ71 〜
75 を総て開き、第2のストップバルブ81 〜85
 を総て閉じ、ガス流量制御手段61 〜65 で制御
して、例えば、ガス吹出しノズル51 及び55 の流
量を2240ccm 、52 及び54 の流量を19
00ccm 、53 の流量を1720ccm にそれ
ぞれ調節してすべてのガス吹出しノズル51 〜55 
から第1のガスを導入し、反応容器12内のガス圧を7
6Torrに保持し、サセプタを50〜60rpm で
回転させながら、 630℃で1μmの厚さのInP層
を成長させた。
[0017] Gas blowing nozzles 51 to 55
When epitaxially forming an InP layer on a growth substrate 4 made of, for example, InP and having a diameter of, for example, 3 inches, the first stop valve 71 to
75, and open the second stop valves 81 to 85.
are all closed and controlled by the gas flow rate control means 61 to 65, for example, the flow rate of the gas blowing nozzles 51 and 55 is set to 2240 ccm, and the flow rate of the gas blowing nozzles 52 and 54 is set to 19 ccm.
The flow rates of 00 ccm and 53 are adjusted to 1720 ccm, respectively, and all gas blowing nozzles 51 to 55 are
The first gas is introduced from
A 1 μm thick InP layer was grown at 630° C. while maintaining the temperature at 6 Torr and rotating the susceptor at 50 to 60 rpm.

【0018】この成長において、3インチ基板4の周辺
3mmを除いた領域におけるエピタキシャル層の膜厚の
分布は±2.5 %以内であった。次いで、直径2イン
チのInPからなる被成長基板上に、この基板上に位置
するガス吹出しノズル52 、53 、54 に3イン
チ基板の場合と同様な流量、即ちノズル52 と54 
に1900ccm 、53 に1720ccm の第1
のガスを流し、第1のストップバルブ71 と75 を
閉じ、第2のストップバルブ81 と85 を開いて、
ガス吹出しノズル51 と55 から、3インチ基板上
への成長の場合の原料を含むガスの流量2240ccm
 とほぼ同流量の成長原料を含まないガス例えば水素[
H2]を導入し、前記3インチ基板の場合と同様な容器
内ガス圧、回転数、温度において、厚さ1μmのInP
層のエピタキシャル成長を行った。
In this growth, the distribution of the film thickness of the epitaxial layer in the region excluding the peripheral 3 mm of the 3-inch substrate 4 was within ±2.5%. Next, on a growth substrate made of InP having a diameter of 2 inches, gas blowing nozzles 52, 53, and 54 located on this substrate are injected with the same flow rate as in the case of a 3-inch substrate, that is, nozzles 52 and 54.
The first of 1900ccm in 53 and 1720ccm in 53
Flow the gas, close the first stop valves 71 and 75, open the second stop valves 81 and 85,
From the gas blowing nozzles 51 and 55, the flow rate of the gas containing the raw material in the case of growth on a 3-inch substrate is 2240 ccm.
A gas that does not contain a growth material at approximately the same flow rate as hydrogen [
H2] was introduced, and at the same gas pressure, rotation speed, and temperature in the container as in the case of the 3-inch substrate, a 1-μm-thick InP
Epitaxial growth of the layers was performed.

【0019】そしてこの成長においても、2インチ基板
の周辺3mmを除いた領域において±2.5 %以内の
膜厚の分布が得られた。またこの成長において、被成長
基板の外側に露出しているサセプタ上に位置するガス吹
出しノズルから導入されるガスは、成長原料を含まない
ガス例えば水素[H2]であるので、露出するサセプタ
上に反応生成物が厚く堆積することはなく、従ってエピ
タキシャル層に反応生成物の剥落飛散粒子による欠陥は
殆ど生じなかった。
Also in this growth, a film thickness distribution within ±2.5% was obtained in the region excluding the peripheral 3 mm of the 2-inch substrate. In addition, in this growth, the gas introduced from the gas blowing nozzle located on the susceptor exposed outside the growth substrate is a gas that does not contain the growth material, such as hydrogen [H2]. The reaction product was not deposited thickly, and therefore, there were almost no defects in the epitaxial layer due to flaking and scattered particles of the reaction product.

【0020】以上の実施例から明らかなように本発明に
係るMOVPE装置においては、大きさの異なる基板に
対しても成長治具を交換せずに同様に均一な厚さを有し
欠陥の少ないエピタキシャル層を成長することができ、
且つまた、成長原料を含むガスの量を、小さい基板上に
成長する際には、それに応じて減少せしめることができ
る。
As is clear from the above examples, in the MOVPE apparatus according to the present invention, substrates of different sizes can be grown with uniform thickness and fewer defects without replacing the growth jig. can grow epitaxial layers,
Additionally, the amount of gas containing the growth material can be correspondingly reduced when growing on smaller substrates.

【0021】なお本発明の構造は、MOVPE装置に限
らず、その他の縦型気相成長装置にも、勿論適用できる
。また、成長原料を含まないガスには、窒素、不活性ガ
ス等も用いられる。
The structure of the present invention is of course applicable not only to the MOVPE apparatus but also to other vertical vapor phase growth apparatuses. Further, nitrogen, inert gas, etc. are also used as the gas that does not contain the growth raw material.

【0022】[0022]

【発明の効果】以上説明のように本発明によれば、如何
なる大きさの被成長基板上へも、成長治具の交換を行わ
ずに均一な膜厚のエピタキシャル層を成長させることが
できるので、装置のダウンタイムを生ぜず、スループッ
トが向上する。
[Effects of the Invention] As explained above, according to the present invention, an epitaxial layer of uniform thickness can be grown on a growth substrate of any size without replacing the growth jig. , throughput is improved without causing equipment downtime.

【0023】また、被成長基板の大きさにほぼ比例して
成長原料を含むガスの流量が決定されるので、余分な原
料を使用せず、製造コストの低減を図りながら膜厚の均
一性の優れたエピタキシャル成長が可能になる。
Furthermore, since the flow rate of the gas containing the growth material is determined approximately in proportion to the size of the substrate to be grown, the uniformity of the film thickness can be improved while eliminating the use of excess materials and reducing manufacturing costs. Excellent epitaxial growth becomes possible.

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

【図1】  本発明の原理説明用模式図[Figure 1] Schematic diagram for explaining the principle of the present invention

【図2】  本
発明の一実施例の縦方向模式断面図
[Fig. 2] A schematic longitudinal cross-sectional view of an embodiment of the present invention

【図3】  従来の
縦型MOVPE装置の縦方向断面模式図
[Figure 3] Schematic longitudinal cross-section of a conventional vertical MOVPE device

【符号の説明】[Explanation of symbols]

1  成長原料を含むガス(第1のガス)の供給管2 
 成長原料を含まないガス(第2のガス)の供給管3 
 サセプタ 4  第1の被成長基板 4′第2の被成長基板 51 〜5n   ガス吹出しノズル 61 〜6n   ガス流量制御手段 71 〜7n   第1のストップバルブ81 〜8n
   第2のストップバルブ91 〜9n   第1の
配管 101 〜10n   第2の配管 11  真空排気口 12  反応容器(反応管) 13  回転軸
1 Supply pipe for gas containing growth raw material (first gas) 2
Supply pipe 3 for gas (second gas) that does not contain growth raw materials
Susceptor 4 First growth substrate 4' Second growth substrate 51 ~ 5n Gas blowing nozzle 61 ~ 6n Gas flow rate control means 71 ~ 7n First stop valve 81 ~ 8n
Second stop valve 91 - 9n First piping 101 - 10n Second piping 11 Vacuum exhaust port 12 Reaction container (reaction tube) 13 Rotating shaft

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】  反応容器内へ一方向からガスを導入す
る複数のガス吹出し口を有し、被成長基板が該ガス吹出
し口に対向して配置される気相成長装置において、成長
原料を含む第1のガスと、成長原料を含まない第2のガ
スとを、個々のガス吹出し口について独立に切り換えて
反応容器内へ導入することを特徴とする気相成長装置。
1. A vapor phase growth apparatus having a plurality of gas outlets for introducing gas into a reaction vessel from one direction, and in which a substrate to be grown is disposed facing the gas outlets, which contains a growth raw material. A vapor phase growth apparatus characterized in that a first gas and a second gas that does not contain a growth material are introduced into a reaction vessel by being switched independently for each gas outlet.
JP10946591A 1991-05-15 1991-05-15 Vapor growth device Pending JPH04337627A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10946591A JPH04337627A (en) 1991-05-15 1991-05-15 Vapor growth device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10946591A JPH04337627A (en) 1991-05-15 1991-05-15 Vapor growth device

Publications (1)

Publication Number Publication Date
JPH04337627A true JPH04337627A (en) 1992-11-25

Family

ID=14510921

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10946591A Pending JPH04337627A (en) 1991-05-15 1991-05-15 Vapor growth device

Country Status (1)

Country Link
JP (1) JPH04337627A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06232060A (en) * 1992-12-11 1994-08-19 Shin Etsu Handotai Co Ltd Method and device for growing epitaxial silicon layer
KR20070004151A (en) * 2005-07-01 2007-01-09 주성엔지니어링(주) Gas injection system and apparatus for fabricating thin film comprising the same
JP2012190903A (en) * 2011-03-09 2012-10-04 Toshiba Corp Vapor phase epitaxial growth device, and vapor phase epitaxial growth method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH06232060A (en) * 1992-12-11 1994-08-19 Shin Etsu Handotai Co Ltd Method and device for growing epitaxial silicon layer
KR20070004151A (en) * 2005-07-01 2007-01-09 주성엔지니어링(주) Gas injection system and apparatus for fabricating thin film comprising the same
JP2012190903A (en) * 2011-03-09 2012-10-04 Toshiba Corp Vapor phase epitaxial growth device, and vapor phase epitaxial growth method
US8835331B2 (en) 2011-03-09 2014-09-16 Kabushiki Kaisha Toshiba Vapor-phase growing apparatus and vapor-phase growing method

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