JPS6034010A - Reaction tube - Google Patents
Reaction tubeInfo
- Publication number
- JPS6034010A JPS6034010A JP58142569A JP14256983A JPS6034010A JP S6034010 A JPS6034010 A JP S6034010A JP 58142569 A JP58142569 A JP 58142569A JP 14256983 A JP14256983 A JP 14256983A JP S6034010 A JPS6034010 A JP S6034010A
- Authority
- JP
- Japan
- Prior art keywords
- reaction tube
- wall
- tube
- gas
- composition
- 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
Links
Classifications
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/24—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials using chemical vapour deposition [CVD]
-
- H—ELECTRICITY
- H10—SEMICONDUCTOR DEVICES; ELECTRIC SOLID-STATE DEVICES NOT OTHERWISE PROVIDED FOR
- H10P—GENERIC PROCESSES OR APPARATUS FOR THE MANUFACTURE OR TREATMENT OF DEVICES COVERED BY CLASS H10
- H10P14/00—Formation of materials, e.g. in the shape of layers or pillars
- H10P14/20—Formation of materials, e.g. in the shape of layers or pillars of semiconductor materials
- H10P14/34—Deposited materials, e.g. layers
- H10P14/3402—Deposited materials, e.g. layers characterised by the chemical composition
- H10P14/3414—Deposited materials, e.g. layers characterised by the chemical composition being group IIIA-VIA materials
- H10P14/3421—Arsenides
Abstract
Description
【発明の詳細な説明】
本発明は薄膜形成装置、就中、気相結晶成長装置におい
て、多層薄膜結晶を形成する際に組成又はドーピング切
換えの急峻な組成又はドーピングの切換えが益々必要に
なってきている。これらの特性を有する薄膜成長装置と
しては、モレキーラービームエビタキシー(略称MBE
)装置がある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a thin film forming apparatus, particularly a vapor phase crystal growth apparatus, in which a steep change in composition or doping is increasingly required when forming a multilayer thin film crystal. ing. A thin film growth device with these characteristics is the molecular beam epitaxy (abbreviated as MBE).
) There is a device.
しかし、M B E法はIQ Torr程度の超高真空
装置を必要とし、保守が容易ではなく、必ずしも量産に
向いているとけ言い碓い。However, the MBE method requires ultra-high vacuum equipment with an IQ Torr level, is not easy to maintain, and is not necessarily suitable for mass production.
常圧又は、それに近い圧力で同等の特性をもつ結晶が気
相成長法で得られるならば、薄膜生産性に関し大巾な向
上が期待される。気相成長法によって薄膜を成長すると
きに、組成切換えの急峻性に影響を及ぼす要素はいくつ
か考えられるが、そのうちの重要なものの一つに反応管
壁への原料ガスの吸着・脱離過程がある。一つの組成(
5)から他の組成(Blへの成長層の切換えを行なうと
き、組成(5)を構成するガスが反応管壁に吸着されて
おり、組成の切換えがおこなわれたのちも、吸収された
組成υ〜関連のガスが反応管内へ脱離し、これが組成(
B)の原料ガスと混入し、組成(鈎を乱すことになる。If crystals with equivalent properties can be obtained by vapor phase growth at or near normal pressure, a significant improvement in thin film productivity is expected. When growing a thin film by vapor phase growth, there are several factors that can affect the steepness of the composition change, and one of the most important is the adsorption/desorption process of the source gas on the reaction tube wall. There is. One composition (
When switching the growth layer from 5) to another composition (Bl), the gas constituting composition (5) is adsorbed on the reaction tube wall, and even after the composition is switched, the absorbed composition The gas associated with υ desorbs into the reaction tube, which changes the composition (
It mixes with the raw material gas of B) and disturbs the composition (hook).
このことによって、一般に気相成長法による薄j漠結晶
の組成切換えは、MBE法に比較して若干劣る結果とな
っている。本発明は上記欠点を改良し組成切換えの急唆
性が確保できる反応管を提供することを目的としており
、反応管壁を2重壁とし内側の壁面に無数の細孔を明け
、2重壁の中間の空間から反応管中心方向に気体を噴出
させて、原料ガスが反応管壁に向うことを妨げる構造と
することによって原料ガスの反応管壁への原料ガスの吸
着・脱離によるメモリー効果を防いでいる。As a result, composition switching of thin crystals using the vapor phase growth method generally results in slightly inferior results compared to the MBE method. The purpose of the present invention is to improve the above-mentioned drawbacks and provide a reaction tube that can ensure rapid composition switching. By ejecting gas from the space in the middle toward the center of the reaction tube and preventing the raw material gas from moving toward the reaction tube wall, a memory effect is achieved due to the adsorption and desorption of the raw material gas onto the reaction tube wall. is prevented.
以下本発明の実施例を図面を使って説明する。Embodiments of the present invention will be described below with reference to the drawings.
第1図f2)は従来の気相成長法の反庸管部分の一例を
示す。この例は有機金属熱分解法の反応管部分を示した
ものであり、反応管人口1より原料ガスが導入され、加
熱した基板ホルダー3上の基板4に向う。反応管入口1
より導入されたガスの一部は基板4に到達する以前に反
応管壁2に吸着される。第1図(b)は第1図(a)の
左半分を拡大した図だあり、組成がAからBに切換わっ
た後の状態を示している。反応管人口1からは、すでに
組成σ3)に対応する原料ガス0が流入して来ているが
、管壁2には、組成(Δ)を成長していたときの原r1
ガス■(一般には複数)が吸着しており、これがゆっく
りと脱離して原料ガス[B]に混入し基板4に向う。FIG. 1 f2) shows an example of the repulsion tube portion of the conventional vapor phase growth method. This example shows a reaction tube portion of the organometallic pyrolysis method, in which raw material gas is introduced from the reaction tube 1 and directed toward the substrate 4 on the heated substrate holder 3. Reaction tube inlet 1
A part of the introduced gas is adsorbed on the reaction tube wall 2 before reaching the substrate 4. FIG. 1(b) is an enlarged view of the left half of FIG. 1(a), and shows the state after the composition has been switched from A to B. From the reaction tube population 1, raw material gas 0 corresponding to the composition σ3) has already flowed in, but on the tube wall 2, the raw material gas 0 corresponding to the composition (Δ) when grown
Gas (generally a plurality of gases) is adsorbed, and this slowly desorbs and mixes with the raw material gas [B] and heads toward the substrate 4.
このため脱離が継続している間は成長組成はこれに対応
して組成[B]でも組成[A]でもない第3の徐々に変
化する組成となる。第2図は本発明の実施例を示すもの
であり、反応管の第1の管壁2の内側に多数の貫通しだ
細孔を稠密に配した第2の管壁2′を第1の管壁の内側
に設けた反応管である。Therefore, while desorption continues, the growth composition correspondingly becomes a third gradually changing composition that is neither composition [B] nor composition [A]. FIG. 2 shows an embodiment of the present invention, in which a second tube wall 2' having a large number of penetrating pores arranged densely inside the first tube wall 2 of the reaction tube is used as the first tube wall 2'. This is a reaction tube installed inside the tube wall.
この例では第20管壁は反応管人口1の首部分1′で第
1の反応管壁と合体させてあるが、反応管入口1及びそ
の上流部分での吸着・脱離が更に問題になる時には、こ
れらの内側にまで第2の管壁を延長させてもよい。第1
の管壁と第2の管壁との間には外部から水素又は窒素又
は不活性ガス等又はそれらの混合ガス(これらガスを総
称して「防護ガス」と称する)を外部から注入する(図
ではCの方向より注入してある)。防護ガスは第2の管
壁に穿たれた細孔より反応管内部に流れるだめ、反応管
壁近傍では反応管壁に垂直方向に反応管の中心に向うガ
ス流が生成されることになる。このだめ組成囚を成長中
に組成(5)関連のガス■が第2の反応管壁に接近しに
くく、管壁へのlIr!1着の確率は著しく小さくなる
。従って、第2図に示すように組成(均の成長にガスを
切り換えた後に組成(5)関連のガスが反応管壁を鋭部
して反l1iS管中に混入することはなく)す、するど
い界面急峻性の組成プロファイルをもつ結晶が得られる
。第3図にけM。、7Ga0.4AsとAl0.1Ga
0.9Asの2層成長の界面近傍の組成切換わりの様子
を示したもので、11は従来の方法r(よる結果で:侶
り、12け本発明になる反応管を用いて成長した結果を
示すものである。In this example, the 20th tube wall is combined with the first reaction tube wall at the neck portion 1' of the reaction tube population 1, but adsorption/desorption at the reaction tube inlet 1 and its upstream portion becomes a further problem. Sometimes the second tube wall may extend inside these. 1st
Between the pipe wall of In this case, it is injected from the direction of C). Since the protective gas flows into the reaction tube through the pores formed in the second tube wall, a gas flow is generated in the vicinity of the reaction tube wall in a direction perpendicular to the reaction tube wall toward the center of the reaction tube. During the growth of this stale composition, the gas related to composition (5) has difficulty approaching the second reaction tube wall, causing lIr! to the tube wall. The probability of finishing first becomes significantly smaller. Therefore, as shown in Figure 2, the gas related to composition (5) does not mix into the anti-l1iS tube through the sharp part of the reaction tube wall after changing the gas to uniform growth. Crystals with compositional profiles with steep interfaces are obtained. Figure 3 Nike M. , 7Ga0.4As and Al0.1Ga
This figure shows the change in composition near the interface during two-layer growth of 0.9As, where 11 shows the results obtained using the conventional method (results obtained using the conventional method), and 12 shows the results obtained using the reaction tube of the present invention. This shows that.
従来法による1?W移I@rl]が約15Aでf)るの
にスイし木装置杖金用いたJ助合には、5八以下の遷移
ハ;1巾となっており、本装置が有効であることを示し
ている。なお、第3図に示した例では成長法は有機金属
熱分解法によるものであり、原料は(CH3)3Al(
CH3)3Ga,AsH3,キャリアガスとしてH2、
防護ガスとして同じくH2を用いている。第2図2にお
いて一2与板ホルダー3は高周波フ11]熱で71)
0 ’0に昇混している。従って成長1M度は、はぼ7
oo’Uである。1 by conventional method? This device is effective because the transition is 58 or less and the width is 1 width when the W transition I@rl is approximately 15A and f) is used. It shows. In the example shown in Figure 3, the growth method is based on organometallic pyrolysis, and the raw material is (CH3)3Al(
CH3)3Ga, AsH3, H2 as carrier gas,
H2 is also used as a protective gas. In Fig. 2, the plate holder 3 is exposed to high frequency heat (71)
It is rising to 0 '0. Therefore, 1M degree of growth is approximately 7
It's oo'U.
以上の実施例は桶型反応管を用いたものであるが、縦型
反IJR管においても同様の効果が期待でき又、他のC
ti b’iの気相成長法にも適用可能である。Although the above examples used a tub-shaped reaction tube, similar effects can be expected with a vertical anti-IJR tube, and other C
It is also applicable to the vapor phase growth method of ti b'i.
第1図ta+は従来の気相成長における反応管を示す図
、第1図(blは第1図(a)の(イ)部分の拡大説明
図、第2図は本発明の実施例の図、第3図はAlGaA
sの成長における従来法及び本発明の実施例による組成
プロファイルの比較図である。第1図〜第3図にむいて
、1・・・・・・・反応管人口、2 ・・反応管管壁、
3………基板ホルダー、4………基板、5………反応管
出口、1′………反応管入口の首部分、2′………第2
の反応管壁、である。2g3図において11(寸従来法
)□でのAJGaAsの組成プロファイル、12は本発
明によるプロファイルを示す。
第1図
CG)
(イ)
(b)
第2図FIG. 1 ta+ is a diagram showing a reaction tube in conventional vapor phase growth, FIG. , Figure 3 shows AlGaA
FIG. 2 is a comparison diagram of composition profiles of a conventional method and an example of the present invention in growing S. For Figures 1 to 3, 1...Reaction tube population, 2...Reaction tube wall,
3...Substrate holder, 4...Substrate, 5...Reaction tube outlet, 1'...Neck part of reaction tube inlet, 2'...Second
is the reaction tube wall. In Figure 2g3, 11 (dimensions conventional method) shows the composition profile of AJGaAs at □, and 12 shows the profile according to the present invention. Figure 1 CG) (a) (b) Figure 2
Claims (1)
の内側に無数の貫通細孔を有する第2の管壁を設け、第
1と第2の管壁の間l:?Aへ気体の導入口を設けたこ
とを特徴とする反応管。A second tube wall having countless through holes is provided inside the first tube wall of the reaction tube in which the thin film is coated on the substrate, and between the first and second tube walls l:? A reaction tube characterized in that A is provided with a gas inlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58142569A JPS6034010A (en) | 1983-08-05 | 1983-08-05 | Reaction tube |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58142569A JPS6034010A (en) | 1983-08-05 | 1983-08-05 | Reaction tube |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6034010A true JPS6034010A (en) | 1985-02-21 |
Family
ID=15318370
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58142569A Pending JPS6034010A (en) | 1983-08-05 | 1983-08-05 | Reaction tube |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6034010A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100450173B1 (en) * | 2001-10-18 | 2004-09-30 | 변철수 | Methods and Apparatuses of Chemical Vapor Deposition using diffusion suppressing gasses and devices |
| US7156921B2 (en) | 2001-10-18 | 2007-01-02 | Chulsoo Byun | Method and apparatus for chemical vapor deposition capable of preventing contamination and enhancing film growth rate |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5421973A (en) * | 1977-07-20 | 1979-02-19 | Cho Lsi Gijutsu Kenkyu Kumiai | Gas phase reaction apparatus |
-
1983
- 1983-08-05 JP JP58142569A patent/JPS6034010A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5421973A (en) * | 1977-07-20 | 1979-02-19 | Cho Lsi Gijutsu Kenkyu Kumiai | Gas phase reaction apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100450173B1 (en) * | 2001-10-18 | 2004-09-30 | 변철수 | Methods and Apparatuses of Chemical Vapor Deposition using diffusion suppressing gasses and devices |
| US7156921B2 (en) | 2001-10-18 | 2007-01-02 | Chulsoo Byun | Method and apparatus for chemical vapor deposition capable of preventing contamination and enhancing film growth rate |
| US7485339B2 (en) | 2001-10-18 | 2009-02-03 | Chulsoo Byun | Method for chemical vapor deposition capable of preventing contamination and enhancing film growth rate |
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