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JPH01222438A - Vapor growth device - Google Patents

Vapor growth device

Info

Publication number
JPH01222438A
JPH01222438A JP4898988A JP4898988A JPH01222438A JP H01222438 A JPH01222438 A JP H01222438A JP 4898988 A JP4898988 A JP 4898988A JP 4898988 A JP4898988 A JP 4898988A JP H01222438 A JPH01222438 A JP H01222438A
Authority
JP
Japan
Prior art keywords
plate
reactor
substrate
gas
thin film
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
JP4898988A
Other languages
Japanese (ja)
Inventor
Keiji Shimizu
清水 啓次
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.)
NEC Corp
Original Assignee
NEC Corp
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 NEC Corp filed Critical NEC Corp
Priority to JP4898988A priority Critical patent/JPH01222438A/en
Publication of JPH01222438A publication Critical patent/JPH01222438A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To relax a difference between a gas flow velocity at the central part of a reactor and a gas flow velocity in the vicinity of the inner wall of the reactor and to improve significantly the uniformity of the film thickness, which is formed within the surface of a substrate, of a grown thin film by a method wherein a shielding plate, whose from and sectional area are equal to the form and sectional area of a raw gas introducing vent, is provided. CONSTITUTION:The title device has a rectifying plate 10 provided with a plurality of fine holes and a shielding plate 11 for shielding the flow of raw gas introduced through a raw gas introducing vent 8 between the plate 10 and the vent 8. In the case a GaAs thin film is grown on a GaAs substrate 1, trimethyl gallium and arsin are introduced in a reactor 2 through the vent 8 after being diluted with hydrogen gas (carrier gas) 7, but the raw gas collides against the plate 11. After that, after passing through the fine holes of the plate 10, the raw gas 5 is fed to the heated substrate and the GaAs thin film 9 is formed by thermal decomposition. Thereby, it can be relaxed for a gas flow velocity at the central part of the reactor to be accelerated and the uniformity of the film thickness of an epitaxially grown layer can be improved.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は気相成長装置に関し、特にエピタキシャル成長
層の面内均一性を改善した縦型気相成長装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a vapor phase growth apparatus, and more particularly to a vertical vapor growth apparatus that improves the in-plane uniformity of an epitaxially grown layer.

〔従来の技術〕[Conventional technology]

従来、この種の気相成長装置は第3図のような構成とな
っている。基板1は石英製の反応炉2の中のサセプター
3の上に載置さり、コイル4で誘起される高周波により
サセプター3を誘導加熱することにより加熱される。原
料ガス5はマスフローコントローラー(MFC)6によ
り流量制御された後にキャリアガス7によって希釈され
て原料ガス導入口8から反応炉2の内部に導入さり。
Conventionally, this type of vapor phase growth apparatus has a configuration as shown in FIG. The substrate 1 is placed on a susceptor 3 in a reactor 2 made of quartz, and is heated by induction heating the susceptor 3 using high frequency waves induced by a coil 4. The raw material gas 5 is flow-controlled by a mass flow controller (MFC) 6, diluted with a carrier gas 7, and introduced into the reactor 2 through a raw material gas inlet 8.

基板1上で熱分解して基板1の上に薄膜9が形成される
。第3図で12はバルブ、13はガス排出口、14は基
板回転機構である。
A thin film 9 is formed on the substrate 1 by thermal decomposition on the substrate 1 . In FIG. 3, 12 is a valve, 13 is a gas outlet, and 14 is a substrate rotation mechanism.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上述した従来の縦型気相成長装置で、例えばトリメチル
ガリウム(Ga (CHs)s:TMG)とアルシン(
AsHs)を原料ガスとして基板1上にG a A r
at薄膜9をエピタキシャル成長を行う場合に、原料ガ
ス5は水素(H2)ガス7に希釈されて原料ガス導入口
8から導入されて、約600℃に加熱されたGaAs基
板1に供給される。基板1が載置される付近の反応炉2
の断面積は原料ガス導入口8よりも大きいため、基板1
付近のガス流速は中央部で速く、反応炉2の内壁付近で
遅いという分布が生じる。そのため成長したG a A
 s薄膜9の膜厚は、第4図に示したようにサセプター
3の中心付近で厚く、周辺部で薄くなるという欠点があ
り、膜厚のバラツキは平均値に対し±12%と大きくな
る欠点があった。そしてこの膜厚の不均一性は基板回転
機構14によって基板を自転させても解消されないとい
う欠点があった。
In the conventional vertical vapor phase growth apparatus described above, for example, trimethyl gallium (Ga(CHs)s:TMG) and arsine (
Ga Ar
When epitaxially growing the at thin film 9, the source gas 5 is diluted with hydrogen (H2) gas 7, introduced through the source gas inlet 8, and supplied to the GaAs substrate 1 heated to about 600°C. Reaction furnace 2 near where the substrate 1 is placed
Since the cross-sectional area of the substrate 1 is larger than that of the raw material gas inlet 8,
A distribution occurs in which the gas flow velocity in the vicinity is fast in the center and slow near the inner wall of the reactor 2. Because of that, G a A has grown
The thickness of the thin film 9 is thick near the center of the susceptor 3 and thinner at the periphery, as shown in FIG. was there. This non-uniformity in film thickness cannot be resolved even if the substrate is rotated by the substrate rotation mechanism 14.

〔課題を解決するための手段〕[Means to solve the problem]

本発明の気相成長装置は、反応炉内部に細孔を設けた整
流板と、断面積が原流ガス導入口の形状及び断面積に等
しい遮蔽板を有している。
The vapor phase growth apparatus of the present invention includes a rectifying plate provided with pores inside the reactor, and a shielding plate whose cross-sectional area is equal to the shape and cross-sectional area of the raw gas inlet.

本発明によれば反応炉の中央部と内壁付近のガス流速の
差を緩和することができる。
According to the present invention, it is possible to alleviate the difference in gas flow velocity between the central portion of the reactor and the vicinity of the inner wall.

〔実施例〕〔Example〕

次に本発明について図面を参照して説明する。 Next, the present invention will be explained with reference to the drawings.

第1図は本発明の一実施例の断面図である。同図におい
て、第3図と同じ番号のものは第3図と同一構成物であ
る。
FIG. 1 is a sectional view of an embodiment of the present invention. In the figure, parts with the same numbers as in FIG. 3 are the same components as in FIG. 3.

従来の縦型気相成長装置と異なる点は、反応炉内部に細
孔を設けた整流板10を原料ガス導入口8とサセプター
3の間に有する点と、原料ガス導入口8と整流板10の
間に遮蔽板11を有する点である。整流板10及び遮蔽
板11は、反応炉2と同じく石英製で、整流板10には
、直径2国の細孔が4mm間隔で一様に設けられている
。又、遮蔽板は原料ガスの流れを遮る位置に配置しであ
る。
The difference from the conventional vertical vapor phase growth apparatus is that a rectifying plate 10 with pores is provided inside the reactor between the raw material gas inlet 8 and the susceptor 3, and that the raw material gas inlet 8 and the rectifying plate 10 This point has a shielding plate 11 between them. The current plate 10 and the shielding plate 11 are made of quartz like the reactor 2, and the current plate 10 has pores with a diameter of 2 mm uniformly provided at intervals of 4 mm. Further, the shielding plate is arranged at a position to block the flow of the raw material gas.

GaAs基板1上にG a A s薄膜を成長させる場
合に、トリメチルガリウムとアルシンは水素ガス7に希
釈された後に原料ガス導入口8から反応炉2内に導入さ
れるが、原料ガスは遮蔽板11に衝突する。その後原料
ガス5は整流板10の細孔を通過してから、約600℃
に加熱したGaAs基板に供給され熱分解によってG 
a A s薄膜9が形成される。尚、整流板10の細孔
の幾何学的な形状の影響を避けるために、基板回転機構
14により毎分lO回回転度以上に基板1を自転させる
必要がある。
When growing a GaAs thin film on a GaAs substrate 1, trimethylgallium and arsine are diluted with hydrogen gas 7 and then introduced into the reactor 2 from the source gas inlet 8, but the source gas is Collision with 11. After that, the raw material gas 5 passes through the pores of the rectifier plate 10, and then heated to approximately 600°C.
G is supplied to a GaAs substrate heated to
An a As thin film 9 is formed. In order to avoid the influence of the geometric shape of the pores of the rectifying plate 10, it is necessary to rotate the substrate 1 by the substrate rotation mechanism 14 at a rotation rate of 10 times or more per minute.

また、遮蔽板11及び整流板10における原料ガス熱分
解は、整流板10とサセプター3との距離を十分に取れ
ば全く生じなかった。
In addition, thermal decomposition of the raw material gas in the shielding plate 11 and the current plate 10 did not occur at all if the distance between the current plate 10 and the susceptor 3 was sufficiently large.

本発明の縦型気相成長装置により3μmの厚さにGaA
s薄膜を成長したときの膜厚のウェハー面内分布を示し
たのが第2図である。基板中心付近の膜厚の増加が抑制
されていて、バラツキは平均値に対して±3%であった
GaA was grown to a thickness of 3 μm using the vertical vapor phase growth apparatus of the present invention.
FIG. 2 shows the distribution of film thickness within the wafer surface when a thin film is grown. The increase in film thickness near the center of the substrate was suppressed, and the variation was ±3% with respect to the average value.

尚、遮蔽板11の断面積を原料ガス導入口8の断面積よ
り大きくすると基板中央部の膜厚が薄くなり、原料ガス
導入口の断面積よりも小さくすると中央部の膜厚が逆に
厚くなり、いずれも均一性は悪くなる傾向を示した。従
って、遮蔽板11の断面積が原料ガス導入口8の断面積
に等しいときが均一性が最も良好であった。
Note that if the cross-sectional area of the shielding plate 11 is made larger than the cross-sectional area of the source gas inlet 8, the film thickness at the center of the substrate becomes thinner, and if it is made smaller than the cross-sectional area of the source gas inlet, the film thickness at the center becomes thicker. In both cases, the uniformity tended to deteriorate. Therefore, the uniformity was the best when the cross-sectional area of the shielding plate 11 was equal to the cross-sectional area of the source gas inlet 8.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、原料ガスの流れを一旦遮
蔽した後に整流板10により原料ガスの流れを調整する
ことにより、反応炉中央部のガス流速が速くなるのを緩
和することができる。したがって、成長した薄膜の基板
内の膜厚の均一性を大幅に向上させることができる効果
がある。
As explained above, in the present invention, by once blocking the flow of the raw material gas and then adjusting the flow of the raw material gas using the baffle plate 10, it is possible to alleviate the increase in the gas flow velocity in the central part of the reactor. Therefore, there is an effect that the uniformity of the thickness of the grown thin film within the substrate can be significantly improved.

また、原料ガスは原料ガス導入口8と整流板10の間で
十分に混合されるため、例えばA l xG&1−XA
S等の混晶を成長させたときの組成比Xの均一性、又は
ドーピングしたときのキャリア濃度の均一性を向上させ
ることができる効果がある。
Moreover, since the raw material gas is sufficiently mixed between the raw material gas inlet 8 and the rectifying plate 10, for example, A l x G & 1-XA
This has the effect of improving the uniformity of the composition ratio X when a mixed crystal such as S is grown, or the uniformity of the carrier concentration when doped.

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

第1図は本発明の一実施例の縦型気相成長装置の断面図
、第2図は本発明の一実施例である第1図に示した縦型
気相成長装置により成長したGaAs薄膜の膜厚の面内
分布図、第3図は、従来の縦型気相成長装置の断面図、
第4図は、従来の縦型気相成長装置により成長したG 
a A s薄膜の膜厚の面内分布図である。 l・・・・・・基板(GaAs基板)、2・・・・・・
反応炉、3・・・・・・サセプター、4・・・・・・コ
イル、5・・・・・・原料ガス、6・・団・マスフロー
コントローラー、7…・・・キャリアガス、8・・・・
・・原料ガス導入口、9・・・・・・薄膜、10・・・
・・・ 整流板、11・・・・・・遮蔽板、12・・・
・・・バルブ、13・・・・・・ガス排出口、14・・
・・・・基板回転機構。 代理人 弁理士 内 原   晋 第1図 基板片!し”力゛うつ距内住×(渠) 第 2 図
FIG. 1 is a cross-sectional view of a vertical vapor phase growth apparatus according to an embodiment of the present invention, and FIG. 2 is a GaAs thin film grown by the vertical vapor phase growth apparatus shown in FIG. 1, which is an embodiment of the present invention. Figure 3 is a cross-sectional view of a conventional vertical vapor phase growth apparatus.
Figure 4 shows G grown using a conventional vertical vapor phase growth apparatus.
FIG. 3 is an in-plane distribution diagram of the film thickness of the a As thin film. l...Substrate (GaAs substrate), 2...
Reactor, 3... Susceptor, 4... Coil, 5... Raw material gas, 6... Mass flow controller, 7... Carrier gas, 8...・・・
... Raw material gas inlet, 9... Thin film, 10...
... Rectifying plate, 11... Shielding plate, 12...
... Valve, 13... Gas discharge port, 14...
...Substrate rotation mechanism. Agent Patent Attorney Susumu Uchihara Figure 1 board piece! Figure 2

Claims (1)

【特許請求の範囲】[Claims]  原料ガスを反応炉内に導入する原料ガス導入口と基板
を載置するサセプターとの間に設けられ複数の細孔を備
えた整流板と前記整流板と前記原料ガス導入口との間に
、前記原料ガス導入口より導入された前記原料ガスの流
れを遮ぎるべく設けられた遮蔽板とを有することを特徴
とする気相成長装置。
A rectifying plate provided with a plurality of pores and provided between a raw material gas inlet for introducing the raw material gas into the reactor and a susceptor on which the substrate is placed, and between the rectifying plate and the raw material gas inlet, A vapor phase growth apparatus comprising: a shielding plate provided to block the flow of the raw material gas introduced from the raw material gas inlet.
JP4898988A 1988-03-01 1988-03-01 Vapor growth device Pending JPH01222438A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4898988A JPH01222438A (en) 1988-03-01 1988-03-01 Vapor growth device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4898988A JPH01222438A (en) 1988-03-01 1988-03-01 Vapor growth device

Publications (1)

Publication Number Publication Date
JPH01222438A true JPH01222438A (en) 1989-09-05

Family

ID=12818637

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4898988A Pending JPH01222438A (en) 1988-03-01 1988-03-01 Vapor growth device

Country Status (1)

Country Link
JP (1) JPH01222438A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5766682A (en) * 1991-12-26 1998-06-16 Tsubouchi; Kazuo Process for chemical vapor deposition of a liquid raw material
CN111235551A (en) * 2020-01-20 2020-06-05 北京北方华创微电子装备有限公司 Susceptor for epitaxial apparatus and epitaxial growth apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5766682A (en) * 1991-12-26 1998-06-16 Tsubouchi; Kazuo Process for chemical vapor deposition of a liquid raw material
CN111235551A (en) * 2020-01-20 2020-06-05 北京北方华创微电子装备有限公司 Susceptor for epitaxial apparatus and epitaxial growth apparatus

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