JPH08335557A - Vapor-phase epitaxial growth apparatus - Google Patents

Vapor-phase epitaxial growth apparatus

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Publication number
JPH08335557A
JPH08335557A JP16015595A JP16015595A JPH08335557A JP H08335557 A JPH08335557 A JP H08335557A JP 16015595 A JP16015595 A JP 16015595A JP 16015595 A JP16015595 A JP 16015595A JP H08335557 A JPH08335557 A JP H08335557A
Authority
JP
Japan
Prior art keywords
gas
gas distributor
epitaxial film
less
particles
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.)
Withdrawn
Application number
JP16015595A
Other languages
Japanese (ja)
Inventor
Masashi Nakamura
正志 中村
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.)
Eneos Corp
Original Assignee
Japan Energy 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 Japan Energy Corp filed Critical Japan Energy Corp
Priority to JP16015595A priority Critical patent/JPH08335557A/en
Publication of JPH08335557A publication Critical patent/JPH08335557A/en
Withdrawn legal-status Critical Current

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Abstract

PURPOSE: To sufficiently control generation of particle of epitaxial film by providing a gas distributor which assures a thermal conductivity which is equal to the specific value or less to a plurality of gas blowing ports provided to guide the reaction gas to a reaction chamber. CONSTITUTION: A vaper-phase epitaxial film is grown using a gas distributor composed of a porous quartz glass plate having the thernal conductivity of 2Wm<-1> K<-1> or less. In this case, the number of particles (particle number larger than 0.6μm<2> or more) after the growth of epitaxial film is ranged from 30 to 50 pieces/cm<2> which is less than one-half of that generated when a gas distributor made of stainless mesh is used. Thereby, the epitaxial film including less particle can be grown.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は半導体結晶の気相エピタ
キシャル成長装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vapor phase epitaxial growth apparatus for semiconductor crystals.

【0002】[0002]

【従来の技術】気相エピタキシャル成長装置において、
半導体基板上に大面積に均一な組成、膜厚を持つ半導体
エピタキシャル層を成長させるためには、反応ガスを半
導体基板上に均一に供給する必要がある。反応ガスを半
導体基板上に均一に供給する方法としては、図3に示す
ように反応ガスを複数のガス吹き出し口4を用いて、基
板保持台2上に基板3が設置された反応室7に導入する
方法がある。
2. Description of the Related Art In a vapor phase epitaxial growth apparatus,
In order to grow a semiconductor epitaxial layer having a uniform composition and a large film thickness on a semiconductor substrate, it is necessary to uniformly supply the reaction gas onto the semiconductor substrate. As a method for uniformly supplying the reaction gas onto the semiconductor substrate, as shown in FIG. 3, the reaction gas is supplied to the reaction chamber 7 in which the substrate 3 is placed on the substrate holder 2 by using a plurality of gas outlets 4. There is a way to introduce.

【0003】[0003]

【発明が解決しようとする課題】しかし、この方法では
ガス吹き出し口4のあるところとないところで圧力差が
生じるためガス吹き出し口4付近でガスの巻きが生じ、
反応ガスによる析出物がガス吹き出し口4付近に付着
し、エピタキシャル膜のパーティクルの発生の原因とな
る。このガスの巻きを防止する方法として、ガス吹き出
し口4にステンレス等の金属製のメッシュ状のガス分配
器6を設ける方法がある(図1)。しかし、この方法でも
エピタキシャル膜のパーティクルの発生を十分に抑える
ことはできなかった。
However, in this method, a pressure difference occurs between the place where the gas outlet 4 is provided and the place where the gas outlet 4 is not provided, so that gas winding occurs near the gas outlet 4.
Precipitates due to the reaction gas adhere to the vicinity of the gas outlet 4 and cause the generation of particles in the epitaxial film. As a method of preventing this gas winding, there is a method of providing a mesh-shaped gas distributor 6 made of metal such as stainless steel at the gas outlet 4 (FIG. 1). However, even with this method, the generation of particles in the epitaxial film could not be sufficiently suppressed.

【0004】本発明の目的は、パーティクルの少ない気
相エピタキシャル膜が成長可能な気相エピタキシャル成
長装置を提供することにある。
An object of the present invention is to provide a vapor phase epitaxial growth apparatus capable of growing a vapor phase epitaxial film containing few particles.

【0005】[0005]

【課題を解決するための手段及び作用】本発明者は、メ
ッシュ部析出物の発生の原因について検討を行った。金
属製のメッシュ状のガス分配器6は熱伝導率が大きいた
め、反応管の周囲から熱を伝えやすく温度が上昇しやす
い。また、メッシュ状のガス分配器を取り付けると、メ
ッシュ部において圧力損失が生じるためメッシュ部分で
の反応ガスのガス対流時間が長くなる。従って、金属製
のメッシュ状のガス分配器6によって反応ガスの温度が
上昇し、反応ガスの一部がメッシュ状のガス分配器6で
分解を起こす。そして、この分解析出物がガス分配器6
のメッシュ部に付着し、そして成膜中に基板上に落下し
てパーティクル発生の原因となる。従って、パーティク
ルの発生を抑えるためには、ガス分配器6のメッシュ部
の温度を上昇させないようにすれば良い。すなわち本発
明は、上記の検討をもとになされたもので、反応ガスを
反応室に導入する複数のガス吹き出し口に熱伝導率が2W
m-1K-1以下のガス分配器を設けたことを特徴とする気相
エピタキシャル成長装置である。
Means and Actions for Solving the Problems The present inventor has examined the cause of the generation of precipitates in the mesh portion. Since the metal mesh-shaped gas distributor 6 has a high thermal conductivity, it is easy to transfer heat from around the reaction tube and the temperature easily rises. Moreover, when a mesh-shaped gas distributor is attached, pressure loss occurs in the mesh portion, so that the gas convection time of the reaction gas in the mesh portion becomes long. Therefore, the temperature of the reaction gas is increased by the metal mesh-shaped gas distributor 6, and a part of the reaction gas is decomposed by the mesh-shaped gas distributor 6. Then, the decomposed deposit is the gas distributor 6
Adheres to the mesh part and falls onto the substrate during film formation, which causes particles. Therefore, in order to suppress the generation of particles, the temperature of the mesh portion of the gas distributor 6 should not be raised. That is, the present invention has been made based on the above-mentioned examination, and the thermal conductivity is 2 W in a plurality of gas outlets for introducing the reaction gas into the reaction chamber.
The vapor phase epitaxial growth apparatus is characterized by being provided with a gas distributor of m -1 K -1 or less.

【0006】メッシュ部の温度を上昇させないようにす
るため、ガス分配器の材料は、温度300Kでの熱伝導率が
2Wm-1K-1以下の材料を用いる。例えば、石英ガラス(熱
伝導率;1.38Wm-1K-1(温度300K))、パイレックスガラス
(熱伝導率;1.10Wm-1K-1(温度300K))、板ガラス(窓用)
(熱伝導率;1.3Wm-1K-1(温度300K))等がガス分配器の材
料として用いることができる。これらの材料を用いて分
配器を形成すれば、反応ガスを加熱することなくガス分
配ができ、分解析出物のガス分配器へ付着を防止し、パ
ーティクルの少ない気相エピタキシャル膜が成長可能に
なる。一方、ステンレス鋼(熱伝導率;14〜17Wm-1K-1(温
度300K))、鉄(熱伝導率;80Wm-1K-1(温度300K))、アルミ
ナ(熱伝導率;36Wm-1K-1(温度300K))、MgO(熱伝導率;60W
m-1K-1(温度300K))等の熱伝導率が2Wm-1K-1より大きい
材料を用いた場合は、ガス分配器に分解析出物が付着し
パーティクルが多く発生するため好ましくない。また、
ガス分配器の構造は、一般的にはメッシュ状であるが、
作製が困難な場合は多孔質板によっても同様の効果が得
られる。
In order to prevent the temperature of the mesh part from rising, the material of the gas distributor has a thermal conductivity at a temperature of 300K.
Materials of 2 Wm -1 K -1 or less are used. For example, quartz glass (thermal conductivity; 1.38 Wm -1 K -1 (temperature 300 K)), Pyrex glass
(Thermal conductivity; 1.10 Wm -1 K -1 (Temperature 300K)), Flat glass (for windows)
(Thermal conductivity; 1.3 Wm -1 K -1 (Temperature 300K)) can be used as the material of the gas distributor. If a distributor is formed using these materials, the gas can be distributed without heating the reaction gas, the decomposition deposits can be prevented from adhering to the gas distributor, and a vapor phase epitaxial film with few particles can be grown. Become. On the other hand, stainless steel (thermal conductivity; 14~17Wm -1 K -1 (temperature 300K)), iron (thermal conductivity; 80Wm -1 K -1 (temperature 300K)), alumina (thermal conductivity; 36Wm -1 K -1 (Temperature 300K), MgO (Thermal conductivity; 60W
When a material having a thermal conductivity of more than 2 Wm -1 K -1 such as m -1 K -1 (temperature 300 K)) is used, decomposition deposits adhere to the gas distributor and many particles are generated, which is preferable. Absent. Also,
The structure of the gas distributor is generally a mesh,
If it is difficult to manufacture, the same effect can be obtained by using a porous plate.

【0007】[0007]

【実施例】【Example】

(実施例)実施例として、図1に示す構造の有機金属気相
エピタキシャル装置によって、InP基板上に1.0μmのIn
Pホモエピタキシャル膜を成長を行った。反応管の構造
を図1に示す。流量計5により制御された反応ガスは、
ガス吹き出し口4、ガス分配器6を介して、反応室7へ
導入される。ガス分配器6として、石英ガラス(熱伝導
率;1.38Wm-1K-1(温度300K))製の多孔質板のガス分配器
を用いた。反応ガスは、トリメチルインジウム(TMI)、
フォスフィン(PH3)を用いた、成長条件は成長温度650
℃、成長圧力30torr、H2流量15 l/min、PH3分圧0.8torr
である。石英ガラス製の多孔質板のガス分配器を用い成
膜実験を3回行った。エピタキシャル膜成長後のパーテ
ィクルの数は、レーザの散乱を利用した表面異物検査装
置によって、0.6μm2以上のパーティクル数をカウント
することで測定した。図3にその結果を示す。石英ガラ
ス製の多孔質板のガス分配器を用いた場合、そのパーテ
ィクルの数(0.6μm2以上のパーティクル数)は30〜50個
/cm2であった。
(Example) As an example, an InP substrate having a structure shown in FIG.
A P homoepitaxial film was grown. The structure of the reaction tube is shown in FIG. The reaction gas controlled by the flow meter 5 is
It is introduced into the reaction chamber 7 through the gas outlet 4 and the gas distributor 6. As the gas distributor 6, a gas distributor having a porous plate made of quartz glass (heat conductivity; 1.38 Wm -1 K -1 (temperature 300 K)) was used. The reaction gas is trimethylindium (TMI),
The growth conditions using phosphine (PH 3 ) are as follows: growth temperature 650
℃, growth pressure 30 torr, H 2 flow rate 15 l / min, PH 3 partial pressure 0.8 torr
Is. A film forming experiment was performed three times using a gas distributor having a porous plate made of quartz glass. The number of particles after the growth of the epitaxial film was measured by counting the number of particles of 0.6 μm 2 or more with a surface foreign matter inspection device using laser scattering. The results are shown in FIG. When a porous glass gas distributor made of quartz glass was used, the number of particles (the number of particles of 0.6 μm 2 or more) was 30 to 50 particles / cm 2 .

【0008】(比較例)実施例と同様に、図1に示す構造
の有機金属気相エピタキシャル装置によって、InP基板
上に1.0μmのInPホモエピタキシャル膜を成長を行っ
た。なお、ガス分配器6として、18-8ステンレス(熱伝
導率;15Wm-1K-1(温度300K))の多孔質板のガス分配器を
用いた。ステンレス製のメッシュのガス分配器を用い、
3回の成膜を行った場合の結果を図3に示す。ステンレ
ス製のメッシュのガス分配器を用いた場合、そのパーテ
ィクルの数(0.6μm2以上のパーティクル数)は70〜100個
/cm2であった。
(Comparative Example) In the same manner as in the example, an InP homoepitaxial film of 1.0 μm was grown on an InP substrate by the metal-organic vapor phase epitaxial device having the structure shown in FIG. As the gas distributor 6, a 18-8 stainless steel (thermal conductivity; 15 Wm -1 K -1 (temperature 300 K)) porous plate gas distributor was used. Using a stainless mesh mesh gas distributor,
The results obtained when the film formation was performed three times are shown in FIG. When a stainless mesh gas distributor is used, the number of particles (the number of particles of 0.6 μm 2 or more) is 70 to 100.
It was / cm 2 .

【0009】このように石英ガラス製の多孔質板のガス
分配器を用いた場合、エピタキシャル膜成長後のパーテ
ィクルの数(0.6μm2以上のパーティクル数)は30〜50個/
cm2とステンレス製のメッシュのガス分配器を用いた場
合の半分以下となっている。以上のことから、熱伝導率
が2Wm-1K-1以下である石英ガラス製の多孔質板のガス分
配器を用いることでパーティクルの少ない気相エピタキ
シャル膜を成長することができることがわかる。
When a gas distributor made of a quartz glass porous plate is used as described above, the number of particles after epitaxial film growth (the number of particles of 0.6 μm 2 or more) is 30 to 50 /
It is less than half that when using a gas distributor with a cm 2 and stainless steel mesh. From the above, it can be seen that a vapor phase epitaxial film with few particles can be grown by using a gas distributor made of a quartz glass porous plate having a thermal conductivity of 2 Wm -1 K -1 or less.

【0010】また、本実施例では石英ガラス製の多孔質
板のガス分配器を用いた有機金属気相エピタキシャル装
置について示したが、パイレックス製の多孔質板のガス
分配器を用いた場合、またメッシュ状の板を用いた場合
でもよい。更には他の気相成長法(例えばハイドライド
法、クロライド法)に用いた場合にも同様に効果があ
る。
Further, in this embodiment, the metal-organic vapor phase epitaxial device using the gas distributor of the porous plate made of quartz glass is shown, but when the gas distributor of the porous plate made of Pyrex is used, It is also possible to use a mesh plate. Further, the same effect can be obtained when it is used in another vapor phase growth method (eg, hydride method, chloride method).

【0011】[0011]

【発明の効果】以上説明したように、本発明の気相エピ
タキシャル成長装置を用いれば、パーティクルの少ない
エピタキシャル膜を成長することが可能である。
As described above, by using the vapor phase epitaxial growth apparatus of the present invention, it is possible to grow an epitaxial film with few particles.

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

【図1】 ガス分配器を用いた気相エピタキシャル装置
の一例を示した図である。
FIG. 1 is a diagram showing an example of a vapor phase epitaxial device using a gas distributor.

【図2】 実施例のエピタキシャル膜成長後の0.6μm2
以上のパーティクル数をカウントした結果を示した図で
ある。
FIG. 2 0.6 μm 2 after growth of the epitaxial film of Example
It is a figure showing the result of having counted the number of particles above.

【図3】 従来の気相エピタキシャル成長装置の一例を
示した図である。
FIG. 3 is a diagram showing an example of a conventional vapor phase epitaxial growth apparatus.

【符号の説明】[Explanation of symbols]

1 加熱装置 2 基板保持台 3 基板 4 ガス導入部 5 流量計 6 ガス分配器 1 Heating Device 2 Substrate Holding Table 3 Substrate 4 Gas Introducing Section 5 Flow Meter 6 Gas Distributor

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 反応ガスを反応室に導入する複数のガス
吹き出し口に熱伝導率が2Wm-1K-1以下のガス分配器を設
けたことを特徴とする気相エピタキシャル成長装置。
1. A vapor phase epitaxial growth apparatus comprising a gas distributor having a thermal conductivity of 2 Wm -1 K -1 or less at a plurality of gas outlets for introducing a reaction gas into a reaction chamber.
JP16015595A 1995-06-05 1995-06-05 Vapor-phase epitaxial growth apparatus Withdrawn JPH08335557A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16015595A JPH08335557A (en) 1995-06-05 1995-06-05 Vapor-phase epitaxial growth apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16015595A JPH08335557A (en) 1995-06-05 1995-06-05 Vapor-phase epitaxial growth apparatus

Publications (1)

Publication Number Publication Date
JPH08335557A true JPH08335557A (en) 1996-12-17

Family

ID=15709068

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16015595A Withdrawn JPH08335557A (en) 1995-06-05 1995-06-05 Vapor-phase epitaxial growth apparatus

Country Status (1)

Country Link
JP (1) JPH08335557A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004510324A (en) * 2000-09-22 2004-04-02 アイクストロン、アーゲー Gas suction element and apparatus for CVD processing
JP4897184B2 (en) * 2000-09-22 2012-03-14 アイクストロン、アーゲー Deposition method and deposition apparatus for depositing a crystal structure layer

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004510324A (en) * 2000-09-22 2004-04-02 アイクストロン、アーゲー Gas suction element and apparatus for CVD processing
JP4897184B2 (en) * 2000-09-22 2012-03-14 アイクストロン、アーゲー Deposition method and deposition apparatus for depositing a crystal structure layer

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