JPH03224215A - Organic metal vapor phase deposition device - Google Patents

Organic metal vapor phase deposition device

Info

Publication number
JPH03224215A
JPH03224215A JP24965490A JP24965490A JPH03224215A JP H03224215 A JPH03224215 A JP H03224215A JP 24965490 A JP24965490 A JP 24965490A JP 24965490 A JP24965490 A JP 24965490A JP H03224215 A JPH03224215 A JP H03224215A
Authority
JP
Japan
Prior art keywords
raw material
material supply
supply system
reactor
mass flow
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
JP24965490A
Other languages
Japanese (ja)
Inventor
Akihiko Kasukawa
秋彦 粕川
Yoshihiro Imasou
義弘 今荘
Hiroshi Okamoto
岡本 紘
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Publication of JPH03224215A publication Critical patent/JPH03224215A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To manufacture the semiconductor elements of a complicated laser structure having excellent characteristics by a method wherein the material feed systems to epitaxially deposit a semiconductor layer on a semiconductor substrate are provided with multiple flow rate controllers. CONSTITUTION:Mixed material gas containing organic metal produced by material feed systems 20, 30, 40, 50, 60. 70 is led into a reactor 10 wherein the mixed material gas is reacted by thermal cracking process to epitaxially deposit a semiconductor layer on a semiconductor substrate 12. AN AsH2 material feed system 20, a PH2 material feed system 30, a TMI material feed system 50 and a TEG material feed system 60 are respectively provided with two each of mass flow controllers 22, three each of mass flow controllers 32, three each of mass flow controllers 51 and two each of mass flow controllers 61. In such a constitution, the composition can be transferred within a short time thereby enabling semiconductor elements of a complicated laser structure having excellent characteristics to be manufactured.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、組成制御性の高い有機金属気相成長装置に関
するものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to an organometallic vapor phase growth apparatus with high composition controllability.

[従来技術; 有機金属気相成長(MOCVD)法は、高周波誘導加熱
によって加熱されたりアクタ内に所望の原料ガスを送り
込み、熱分解反応によって前記リアクタ内に配置された
半導体基板上に所望の半導体層をエビタキャル成長させ
る成長法であり、その特徴として、大面積にわたり組成
・膜厚の良好なエピタキシャル層を容易に得ることがで
きる特徴を有する。この基本的な装置を第3図に示す。
[Prior art; In the metal organic chemical vapor deposition (MOCVD) method, a desired raw material gas is heated by high-frequency induction heating or fed into an reactor, and a desired semiconductor is formed on a semiconductor substrate placed in the reactor by a thermal decomposition reaction. This is a growth method in which a layer is grown epitaxially, and its feature is that an epitaxial layer with good composition and film thickness can be easily obtained over a large area. This basic device is shown in FIG.

図において、10は石英製のりアクタ、11は高周波誘
導加熱用コイル、12はI nGaのような半導体基板
、20はAsH,原料供給系、30はPH3原料供給系
、40はHlS、原料供給系、50は有機金属系のトリ
メチルインジウム(TMI)原料供給系、60はトリエ
チルガリウム(TEG)原料供給系、70はP型ドーパ
ントとなるディエチルジインク(DEZ)原料供給系、
80は原料供給系配管、90は原料供給圧力補正用配管
である。100は石英製のりアクタ10内を真空状態に
保持するロータリポンプ、101はロータリボノブ10
0内の油等の汚染物質を石英製のりアクタlO側に逆流
しないようにするトラップ装置である。ここでAsH,
原料供給系20は、AsH=ガスを収納したA5H3ボ
ンへ21、このガスの流用制御を行うマスフローコント
ローラ22、及び原料供給系管路80と原料供給圧力補
正用配管90とにそれぞれ接続し、マスフローコントロ
ーラ22からのガスの流れをリアクタ10内に導入・非
導入するバルブ23.24とで構成され、原料供給圧力
補正用配管90を介して、マスフローコントローラ22
によって流量制御されたAsH3を石英製リアクタ10
に導くようになっている。またPH,原料供給系30及
びHls、原料供給系40も同様に、PH3ボンベ31
、Hls、ボンへ41、マスフローコントローラ32.
42、バルブ33.34.43.44により構成され、
同様にして各原料を石英製リアクタ10に導くようにな
っている。またTMI原料供給系50は図示しない水素
ガス供給源からの水素を流量制御するマスフローコント
ローラ51.TMI原料を収納したバブリング装置52
、原料供給系配管80及び原料供給圧力補正用配管90
にそれぞれ接続されたバブル53.54とで構成され、
マスフローコントローラ51で流量制御された水素をハ
フリング装置52内に導き、ここで水素をTM+原料内
でバブリングさせることによって、水素中にTMI原料
が包含したガスを作成し、この作成されたガスをバルブ
53を介してリアクタ10内に導くようになっている。
In the figure, 10 is a quartz glue actuator, 11 is a high-frequency induction heating coil, 12 is a semiconductor substrate such as InGa, 20 is an AsH, raw material supply system, 30 is a PH3 raw material supply system, 40 is a HlS, raw material supply system , 50 is an organometallic trimethylindium (TMI) raw material supply system, 60 is a triethyl gallium (TEG) raw material supply system, 70 is a diethyl diink (DEZ) raw material supply system that becomes a P-type dopant,
80 is a raw material supply system pipe, and 90 is a raw material supply pressure correction pipe. 100 is a rotary pump that maintains the inside of the quartz glue actuator 10 in a vacuum state, and 101 is a rotary ribbon knob 10.
This is a trap device that prevents contaminants such as oil from flowing back into the quartz glue actuator IO side. Here AsH,
The raw material supply system 20 is connected to an A5H3 cylinder 21 containing AsH=gas, a mass flow controller 22 that controls the flow of this gas, a raw material supply system pipe 80, and a raw material supply pressure correction pipe 90, and is connected to the mass flow The mass flow controller 22 is configured with valves 23 and 24 for introducing or not introducing the gas flow from the controller 22 into the reactor 10, and is connected to the mass flow controller 22 via the raw material supply pressure correction piping 90.
The flow rate of AsH3 was controlled by the quartz reactor 10.
It is designed to lead to. Similarly, the PH, raw material supply system 30 and Hls, raw material supply system 40 are connected to the PH3 cylinder 31.
, Hls, Bonhe 41, mass flow controller 32.
42, consisting of valves 33.34.43.44;
In the same manner, each raw material is guided to the quartz reactor 10. The TMI raw material supply system 50 also includes a mass flow controller 51 that controls the flow rate of hydrogen from a hydrogen gas supply source (not shown). Bubbling device 52 containing TMI raw material
, raw material supply system piping 80 and raw material supply pressure correction piping 90
consisting of bubbles 53 and 54 respectively connected to
Hydrogen whose flow rate is controlled by the mass flow controller 51 is guided into the Huffling device 52, where the hydrogen is bubbled within the TM+ raw material to create a gas containing the TMI raw material in the hydrogen, and this created gas is passed through the valve. 53 into the reactor 10.

TEG原料供給系60及びDEZ原料供給系70も同様
にしてマスフローコントローラ61.71.バブリング
装置62.72、バブル63.64.73.74とで構
成されている。原料供給系配管80及び原料供給圧力補
正用配管90にはそれぞれマスフローコントローラ81
・91を介して水素及び窒素の混合ガスが所定量供給さ
れ、各原料供給系に接続されたバブルの開閉によってこ
れら配管に生ずる圧力の変化を吸収するように構成され
ている。なお110は各マスフローコントローラ及びバ
ルブを制御するためのコンピュータである。
The mass flow controllers 61, 71. It is composed of a bubbling device 62.72 and bubbles 63.64.73.74. A mass flow controller 81 is provided in each of the raw material supply system piping 80 and the raw material supply pressure correction piping 90.
- A predetermined amount of a mixed gas of hydrogen and nitrogen is supplied through the pipe 91, and it is configured to absorb changes in pressure occurring in these pipes by opening and closing bubbles connected to each raw material supply system. Note that 110 is a computer for controlling each mass flow controller and valve.

このような装置において、半導体基板12上に有機金属
膜を気相成長させるには、まず初め、ロータリポンプ1
00を動作させてリアクタ10内を所定の真空圧力状態
にするとともに、高周波誘導加熱用コイル11に通電し
、リアクタ10内の半導体基板12を所定温度、例えば
650℃に加熱しておく。この状態で前記AsHs原料
供給系20、PH3原料供給系30、Hz S −原料
供給系40、TMI原料供給系50、TEG原料供給系
60、DEZ原料供給系70を各マスフローコントロー
ラによって流、量制御し、各系統のバルブ及び原料供給
系配管80を介して石英製リアクタ10に導かれる0石
英製リアクタ10に導かれた混合原料ガスはここで熱分
解反応し、半導体基板12上にエピタキシャル成長によ
る所定組成比の有機金属膜が積層される。エピタキシャ
ル成長による有機金属膜の組成比を変化させるには、予
めコンピュータ110に記憶されたプログラムによって
、前記マスフローコントローラの流量及び各ノ1ルブを
制御することによってなされる。混合原料ガスが熱分解
反応した残りのガスは、ロータリポンプ100を介して
、図示しない排気ガス処理装置に排出される。
In such an apparatus, in order to grow an organometallic film on the semiconductor substrate 12 in a vapor phase, first, the rotary pump 1 is
00 is operated to bring the inside of the reactor 10 into a predetermined vacuum pressure state, and the high-frequency induction heating coil 11 is energized to heat the semiconductor substrate 12 inside the reactor 10 to a predetermined temperature, for example, 650°C. In this state, the flow and quantity of the AsHs raw material supply system 20, PH3 raw material supply system 30, Hz S - raw material supply system 40, TMI raw material supply system 50, TEG raw material supply system 60, and DEZ raw material supply system 70 are controlled by each mass flow controller. The mixed raw material gas guided to the quartz reactor 10 through the valves of each system and the raw material supply system piping 80 undergoes a thermal decomposition reaction here, and a predetermined amount is formed on the semiconductor substrate 12 by epitaxial growth. Organometallic films with different composition ratios are stacked. The composition ratio of the organic metal film formed by epitaxial growth is changed by controlling the flow rate and each knob of the mass flow controller using a program stored in the computer 110 in advance. The remaining gas resulting from the thermal decomposition reaction of the mixed raw material gas is discharged to an exhaust gas treatment device (not shown) via the rotary pump 100.

このようなMOCVD法は近年盛んに行われている。特
に、光通信用光源として重要であるGaInAsP/I
nP系においてMOCVD法は有効な成長法である。G
a InAsP/InP系において分離閉じ込めヘテロ
(SCH)構造の多重量子井戸レーザが作製され、動特
性において量子井戸レーザに期待される特性の改善が得
られている。
Such MOCVD method has been widely used in recent years. In particular, GaInAsP/I, which is important as a light source for optical communication,
MOCVD is an effective growth method for nP systems. G
A multi-quantum well laser with a separate confinement heterostructure (SCH) structure has been fabricated in the InAsP/InP system, and improvements in dynamic characteristics expected for quantum well lasers have been obtained.

[従来技術の課題] 従来のMOCVD装置は、一つの原料に対し、−個の流
量制御器を備えていた。
[Problems with the Prior Art] A conventional MOCVD apparatus was equipped with - number of flow rate controllers for one raw material.

一方、このMOCVD法を用い作成できる半導体レーザ
素子の一つに、A A xGa+−、As/GaAs系
がある。この材料系の場合、エピタキシャル成長温度で
はA i Xca+−xAsliとGaAsFiとでは
、格子不整合が殆ど無い。従って、GaAs層、A 1
 、Ga、−、As層、GaAs層、A 1 vGa+
−JS層、GaAs層、^’ zGa+−zAslii
・・・と言った複数層をエピタキシャル成長する場合、
それぞれのエピタキシャル成長界面でガス切り換えのた
め生しる組成の異なるNC遷移層)が存在するが、互い
に隣合う組成の格子不整合が非常に小さいので、レーザ
特性への影響が殆ど生しない。
On the other hand, one of the semiconductor laser devices that can be produced using this MOCVD method is A A x Ga+-, As/GaAs system. In the case of this material system, there is almost no lattice mismatch between A i Xca+-xAsli and GaAsFi at the epitaxial growth temperature. Therefore, the GaAs layer, A 1
, Ga, −, As layer, GaAs layer, A 1 vGa+
-JS layer, GaAs layer, ^' zGa+-zAslii
When epitaxially growing multiple layers such as...
Although there is an NC transition layer with a different composition due to gas switching at each epitaxial growth interface, since the lattice mismatch between adjacent compositions is very small, it hardly affects the laser characteristics.

しかしながら、Gaxln+−xAsyP+−y/In
P系では、遷移層が数〜数十人程度存在すると、Ga1
nAsP系の結晶性が劣化し、レーザ特性に影響を及ぼ
す。特に、量子井戸レーザ素子のように、−層の厚さが
数十〜数百人と非常に薄い場合には、更に顕著になる。
However, Gaxln+-xAsyP+-y/In
In the P system, if there are several to several dozen transition layers, Ga1
The crystallinity of the nAsP system deteriorates, affecting laser characteristics. In particular, this becomes more noticeable when the thickness of the -layer is very thin, from several tens to several hundreds, as in a quantum well laser device.

また組成の異なるGalnAsP層を、一つのますフロ
ーコントローラで制御した場合、流量に関し大きなグイ
ナミノクレンジが必要となり、精度上から組成制御性が
問題となる。従って、これまでのMOCVD装置では、
Ga1nAsP/TnP系に関しては、複雑な層構造の
エピタキシャル成長ができず、SCH構造に限られ、し
きい値電流密度の低減を実現することができなかった。
Furthermore, when GalnAsP layers having different compositions are controlled by one mass flow controller, a large flow rate is required, and composition controllability becomes a problem from the viewpoint of accuracy. Therefore, with conventional MOCVD equipment,
Regarding the Ga1nAsP/TnP system, it was not possible to epitaxially grow a complex layer structure, and it was limited to the SCH structure, and it was not possible to realize a reduction in threshold current density.

[課題を解決するための手段] 本発明はかかる点に迄みなされたもので、その目的は、
優れた特性を有する半導体レーザが作製可能なMOCV
D装置を提供することにあり、その具体的な構成は、複
数の原料供給系によって作成された有機金属を含む混合
原料ガスをリアクタ内に導き、リアクタ内で前記混合原
料ガスを熱分解反応させることによって半導体層をエピ
タキシャル成長させる有機金属気相成長装置において、
少なくとも一つの前記原料供給系が複数の流量側m器を
備えていることを特徴とする有機金属気相成長装置であ
る。
[Means for Solving the Problems] The present invention has been conceived up to this point, and its purpose is to:
MOCV enables production of semiconductor lasers with excellent characteristics
D apparatus is provided, and its specific configuration is to introduce a mixed raw material gas containing an organic metal produced by a plurality of raw material supply systems into a reactor, and cause the mixed raw material gas to undergo a thermal decomposition reaction within the reactor. In an organometallic vapor phase growth apparatus that epitaxially grows a semiconductor layer by
The metal-organic vapor phase growth apparatus is characterized in that at least one of the raw material supply systems is equipped with a plurality of flow rate side devices.

〔実施例〕〔Example〕

本発明の一実施例を第1図に示す。図において第3図で
説明したと同一のlO〜110は、それぞれ第3図に示
す場合と同一物を示し、その機能も同一である。しかし
ながらHg5a原料供給系40及びDEZ原料供給系7
0を除く各原料供給系20〜60は次の点において異な
っている。即ち、A s Hs原料供給系管路は、マス
フローコントローラ22を2個備え、さらに各マスフロ
ーコントローラ22には供給系配管80と原料供給圧力
補正用配管90とにそれぞれバルブ23・24を備えて
いる。PH3原料供給系30は、マスフローコントロー
ラ32を3個備えており、各マスフローコントローラ3
2には、供給系配管80と原料供給圧力補正用配管90
とにそれぞれバルブ33・34を備えている。しかしな
がら、図面には図を簡単にするため、各装置等を重ねて
表示している(以下の説明においても同し)、TMI原
料供給系50は、3個のマスフローコントローラ51を
備え、各マスフローコントローラ51には、それぞれバ
ブリング装置52が接続され、各バブリング装置52に
は原料供給系管路80と原料供給圧力補正用配管90と
にそれぞれ接続されたバルブ53・54とを備えている
。同様にして、TEGI料供給糸供給系60個のマスフ
ローコントローラ61.2個のバブリング装置62、及
び各バブリング装置62に接続されたバルブ63・64
とを備えている。
An embodiment of the present invention is shown in FIG. In the figure, IO to 110 which are the same as those explained in FIG. 3 respectively indicate the same parts as shown in FIG. 3, and their functions are also the same. However, Hg5a raw material supply system 40 and DEZ raw material supply system 7
Each of the raw material supply systems 20 to 60 except for 0 differs in the following points. That is, the A s Hs raw material supply system pipe line is equipped with two mass flow controllers 22, and each mass flow controller 22 is equipped with valves 23 and 24 on the supply system pipe 80 and the raw material supply pressure correction pipe 90, respectively. . The PH3 raw material supply system 30 includes three mass flow controllers 32, and each mass flow controller 3
2 includes a supply system piping 80 and a raw material supply pressure correction piping 90.
and valves 33 and 34, respectively. However, in order to simplify the drawing, each device is shown in an overlapping manner (the same applies in the following explanation).The TMI raw material supply system 50 includes three mass flow controllers 51, and each mass flow A bubbling device 52 is connected to each controller 51, and each bubbling device 52 includes valves 53 and 54 connected to a raw material supply system pipe line 80 and a raw material supply pressure correction pipe 90, respectively. Similarly, 60 mass flow controllers 61, 2 bubbling devices 62, and valves 63 and 64 connected to each bubbling device 62 of the TEGI material supply yarn supply system.
It is equipped with

本装置を実際に使用するには、まず初め、従来と同様に
、高周波誘導加熱用コイル11に通電し、リアクタ10
内の半導体基板12を所定温度、例えば650℃に加熱
しておく。この状態で前記ASH1原料供給系20、P
H3原料供給系30、Hz S−原料供給系40、TM
[原料供給系50、TEG原料供給系60、DEZ原料
供給系70の何れか1つ又は複数の各マスフローコント
ローラによって流量制御し、各系統の1つのバルブを介
して、各原料供給系20〜70からリアクタ10内に所
定混合比の混合原料ガスを供給し、従来と同様にリアク
タ10内でMOCVD反応をさせる。
To actually use this device, first of all, as in the conventional case, the high-frequency induction heating coil 11 is energized, and the reactor 10 is energized.
The semiconductor substrate 12 inside is heated to a predetermined temperature, for example, 650°C. In this state, the ASH1 raw material supply system 20, P
H3 raw material supply system 30, Hz S-raw material supply system 40, TM
[The flow rate is controlled by one or more mass flow controllers of the raw material supply system 50, the TEG raw material supply system 60, and the DEZ raw material supply system 70, and each raw material supply system 20 to 70 is controlled through one valve of each system. A mixed raw material gas having a predetermined mixing ratio is supplied into the reactor 10 from the reactor 10, and an MOCVD reaction is caused in the reactor 10 as in the conventional method.

この状態でリアクタ10に供給する原料組成を変化させ
るときは予め他の使用していないマスフローコントロー
ラを介して供給しようとする各原料供給系の流量を個々
に制御して原料供給圧力補正用配管90に接続した各バ
ルブを介して排出させておき、この状態で各原料供給系
のバルブを開閉制御することにより、これまで供給して
いた原料を原料供給圧力補正用配管90側に排出させる
とともに、前記原料供給圧力補正用配管90側に排出さ
れていた原料を供給系配管80側に切り換える。これに
より予め調整された適性な量の各原料を瞬時に切り換え
ることができる。従って極めて短時間にして適性な量お
よび混合比の原料ガスをリアクタ10内に供給すること
ができる。これらの制御は予めプログラミングさせたコ
ンピュータ110により各層を形成する毎に順次行われ
る。
When changing the raw material composition to be supplied to the reactor 10 in this state, the flow rate of each raw material supply system to be supplied is individually controlled via other unused mass flow controllers, and the raw material supply pressure correction piping 90 By controlling the opening and closing of the valves of each raw material supply system in this state, the raw materials that have been supplied so far are discharged to the raw material supply pressure correction piping 90 side, and The raw material discharged to the raw material supply pressure correction piping 90 side is switched to the supply system piping 80 side. This makes it possible to instantly switch between appropriate amounts of each raw material that have been adjusted in advance. Therefore, a suitable amount and mixing ratio of raw material gas can be supplied into the reactor 10 in a very short period of time. These controls are sequentially performed each time each layer is formed by a computer 110 programmed in advance.

第2図は下記表の条件に基づき本装置により製造された
半導体レーザ素子を示す。図において、121はn−1
nP基板、122はn−1nPバツフア一層、123は
量子井戸活性層、124及び125はそれぞれ活性層1
23よりバンドギャップの大きな四元層からなるノンド
ープ閉じ込め層、126はp−1nPクラッド層、12
7はp−Ga1nAsPコンタクト層である。閉し込め
層124及び125の組成は活性層123に近い方から
バンドギャップ波長に換算して1.1.1.051.0
.0.95μmとした。また、量子井戸活性層123は
バンドギャップ波長に換算して1.32μm組成の量子
井戸(厚さ150人)、バンドギャップ波長に換算して
1.1μmMi成の障壁層(厚さ1 50人)から成っている。
FIG. 2 shows a semiconductor laser device manufactured by this apparatus based on the conditions shown in the table below. In the figure, 121 is n-1
nP substrate, 122 is an n-1nP buffer layer, 123 is a quantum well active layer, 124 and 125 are each active layer 1
126 is a p-1nP cladding layer;
7 is a p-Ga1nAsP contact layer. The composition of the confinement layers 124 and 125 is 1.1.1.051.0 in terms of bandgap wavelength from the side closest to the active layer 123.
.. It was set to 0.95 μm. In addition, the quantum well active layer 123 includes a quantum well (thickness: 150 μm) having a composition of 1.32 μm in terms of band gap wavelength, and a barrier layer (thickness: 150 μm) having a composition of 1.1 μm in terms of band gap wavelength. It consists of

表 この得られた半導体レーザ素子のしきい値電流密度は井
戸数5.共振器長890μmの全面電極型の構造で0.
41KA/Cm”とこれまで報告のあった中で最も低い
値を実現した。
The threshold current density of the semiconductor laser device obtained in the table is 5. Full-surface electrode structure with a resonator length of 890 μm.
41KA/Cm", the lowest value ever reported.

[発明の効果コ 本発明は上記のように、複数の原料供給系によって作成
された有機金属を含む混合原料ガスをリアクタ内に導き
、リアクタ内で前記混合原料ガスを熱分解反応させるこ
とによって、リアクタ内に配置された半導体基板上に半
導体層をエピタキシャル成長させる有機金属気相成長装
置において、少なくとも1つの原料供給系にそれぞれ独
立に設定可能な流量制御器を複数個設置したことを特徴
とする有機金属気相成長装置である。このため、短時間
して厳密な組成の制御切り換えを必要とする混晶半導体
の超薄膜へテロ接合を単原子オーダの界面急峻性をもっ
て製作することが可能となり、優れた特性を有する複雑
なレーザ構造の半導体素子を提供することができる優れ
た効果がある。
[Effects of the Invention] As described above, the present invention introduces a mixed raw material gas containing an organic metal produced by a plurality of raw material supply systems into a reactor, and causes the mixed raw material gas to undergo a thermal decomposition reaction in the reactor. A metal organic vapor phase growth apparatus for epitaxially growing a semiconductor layer on a semiconductor substrate placed in a reactor, characterized in that at least one raw material supply system is provided with a plurality of independently settable flow rate controllers. This is a metal vapor phase growth device. This makes it possible to fabricate ultra-thin film heterojunctions of mixed crystal semiconductors with interface steepness on the order of single atoms, which requires precise compositional switching in a short period of time. This has an excellent effect of providing a semiconductor device with a structured structure.

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

第1図は本発明の一実施例のMOCVD装置、第2図は
本発明の装置を用いて作製された半導体レーザ素子の構
造模式図、第3図は従来のMOCVD装置を示す構成図
である。 10は石英製のりアクタ、11は高周波誘導加熱用コイ
ル、12は半導体基板、20はAsH3原料供給系、3
0はPH3原料供給系、40はH,S。 原料供給系、50は有機金属系のトリメチルインジウム
(TMI)原料供給系、60はトリエチルガリウム(T
EG)原料供給系、70はDEZ原料供給系、80は原
料供給系配管、90は原料供給圧力補正用配管である。
FIG. 1 is an MOCVD device according to an embodiment of the present invention, FIG. 2 is a schematic structural diagram of a semiconductor laser device manufactured using the device of the present invention, and FIG. 3 is a configuration diagram showing a conventional MOCVD device. . 10 is a quartz glue actor, 11 is a high-frequency induction heating coil, 12 is a semiconductor substrate, 20 is an AsH3 raw material supply system, 3
0 is the PH3 raw material supply system, 40 is H, S. A raw material supply system, 50 is an organometallic trimethylindium (TMI) raw material supply system, 60 is a triethyl gallium (T
EG) Raw material supply system, 70 is a DEZ raw material supply system, 80 is a raw material supply system piping, and 90 is a raw material supply pressure correction piping.

Claims (2)

【特許請求の範囲】[Claims] (1)複数の原料供給系によって作成された有機金属を
含む混合原料ガスをリアクタ内に導き、リアクタ内で前
記混合原料ガスを熱分解反応させることによって、リア
クタ内に配置された半導体基板上に半導体層をエピタキ
シャル成長させる有機金属気相成長装置において、少な
くとも一つの前記原料供給系が複数の流量制御器を備え
ていることを特徴とする有機金属気相成長装置。
(1) A mixed raw material gas containing organic metals created by multiple raw material supply systems is introduced into the reactor, and the mixed raw material gas is subjected to a thermal decomposition reaction in the reactor, thereby forming a material on a semiconductor substrate placed in the reactor. A metal organic vapor phase growth apparatus for epitaxially growing a semiconductor layer, wherein at least one of the raw material supply systems is equipped with a plurality of flow rate controllers.
(2)一つの原料供給系に設けられた複数の流量制御器
には、それぞれの流量制御器によって流量制御された原
料ガスをリアクタ内に導入・非導入するバルブが設けら
れていることを特徴とする請求項1記載の有機金属気相
成長装置。
(2) A plurality of flow rate controllers provided in one raw material supply system are provided with valves for introducing or not introducing the raw material gas whose flow rate is controlled by each flow rate controller into the reactor. The organometallic vapor phase growth apparatus according to claim 1.
JP24965490A 1989-12-27 1990-09-19 Organic metal vapor phase deposition device Pending JPH03224215A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP1-339537 1989-12-27
JP33953789 1989-12-27

Publications (1)

Publication Number Publication Date
JPH03224215A true JPH03224215A (en) 1991-10-03

Family

ID=18328413

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24965490A Pending JPH03224215A (en) 1989-12-27 1990-09-19 Organic metal vapor phase deposition device

Country Status (1)

Country Link
JP (1) JPH03224215A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012092414A (en) * 2010-10-29 2012-05-17 Ulvac Japan Ltd Gas supply system

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012092414A (en) * 2010-10-29 2012-05-17 Ulvac Japan Ltd Gas supply system

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