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JPH0727868B2 - Vapor phase growth equipment - Google Patents
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JPH0727868B2 - Vapor phase growth equipment - Google Patents

Vapor phase growth equipment

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Publication number
JPH0727868B2
JPH0727868B2 JP62099147A JP9914787A JPH0727868B2 JP H0727868 B2 JPH0727868 B2 JP H0727868B2 JP 62099147 A JP62099147 A JP 62099147A JP 9914787 A JP9914787 A JP 9914787A JP H0727868 B2 JPH0727868 B2 JP H0727868B2
Authority
JP
Japan
Prior art keywords
gas
substrate
phase growth
vapor phase
vapor
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.)
Expired - Fee Related
Application number
JP62099147A
Other languages
Japanese (ja)
Other versions
JPS63263718A (en
Inventor
功 松本
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.)
Taiyo Nippon Sanso Corp
Original Assignee
Nippon Sanso 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 Nippon Sanso Corp filed Critical Nippon Sanso Corp
Priority to JP62099147A priority Critical patent/JPH0727868B2/en
Publication of JPS63263718A publication Critical patent/JPS63263718A/en
Publication of JPH0727868B2 publication Critical patent/JPH0727868B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Chemical Vapour Deposition (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は気相成長ガスを基板面と平行に流して成膜基板
を得る気相成長装置に関する。
TECHNICAL FIELD The present invention relates to a vapor phase growth apparatus for obtaining a film formation substrate by flowing a vapor phase growth gas in parallel with a substrate surface.

〔従来の技術〕[Conventional technology]

前記成膜基板は気相成長ガス中の原料ガスが熱化学反応
し反応生成物が基板面に堆積して成長膜を形成すること
によって得られる。この場合、本発明における気相成長
ガスとは少なくとも1種類の原料ガスH2(水素),He
(ヘリウム),Ar(アルゴン),N2(窒素)等の稀釈ガ
スで稀釈したガスであり、また、原料ガスとは気相成長
反応に寄与する個々の成分ガスで、たとえばSiH4(シラ
ン),AsH3(アルシン),TMG(トリメチルガリウム)蒸
気等である。
The film-forming substrate is obtained by forming a growth film by thermochemically reacting the raw material gas in the vapor-phase growth gas and depositing a reaction product on the substrate surface. In this case, the vapor growth gas in the present invention means at least one source gas H 2 (hydrogen), He.
(Helium), Ar (argon), N 2 (nitrogen), and other gases diluted with a diluting gas. The source gas is an individual component gas that contributes to the vapor phase growth reaction, such as SiH 4 (silane). , AsH 3 (arsine), TMG (trimethylgallium) vapor, etc.

原料ガスは目的に応じ単独で、または混合して使用さ
れ、例えばGaAs(ガリウムヒ素)基板にGaAs膜を形成す
るときは、AsH3とTMG蒸気の両原料ガスをH2で稀釈した
気相成長ガスを用いる。以下、図面を用いて従来の気相
成長装置の一例を説明する。
The source gases are used alone or as a mixture depending on the purpose. For example, when forming a GaAs film on a GaAs (gallium arsenide) substrate, both AsH 3 and TMG vapor source gases are diluted with H 2 for vapor phase growth. Use gas. An example of a conventional vapor phase growth apparatus will be described below with reference to the drawings.

第3図は従来の気相成長装置の断面図で、1は筒状の反
応管である。反応管1は、一端に気相成長ガス導入管2
を、他端にガス排出管3を有すると共に、内部に保持台
(サセプタ)4が設けられ、該保持台4の気相成長ガス
導入管2側には気相成長ガスの流れを円滑にするための
フローチャンネル5が設けられている。なお、6は反応
管1の外周に設けたRFコイルである。
FIG. 3 is a sectional view of a conventional vapor phase growth apparatus, and 1 is a cylindrical reaction tube. The reaction tube 1 has a vapor growth gas introduction tube 2 at one end.
Has a gas discharge pipe 3 at the other end, and a holding table (susceptor) 4 is provided inside, and the vapor growth gas introduction pipe 2 side of the holding table 4 smoothes the flow of the vapor growth gas. A flow channel 5 is provided. Incidentally, 6 is an RF coil provided on the outer circumference of the reaction tube 1.

このように構成された従来装置において、未処理の基板
7を保持台4に載せた後、RFコイル6により保持台4を
加熱し、該保持台4を介して基板7を所定の高温に保持
すると共に、気相成長ガスを気相成長ガス導入管2から
反応管1内に横方向に導入し、反応管1内に設けた保持
台4上に載置した基板7面上に流す。この操作によって
気相成長ガスは反応管1内を基板7面と平行に流れ、基
板7近傍の高温部で熱分解して反応生成物が基板7面上
に堆積し成長膜が形成される。
In the conventional apparatus thus configured, the unprocessed substrate 7 is placed on the holding table 4, the holding table 4 is heated by the RF coil 6, and the substrate 7 is held at a predetermined high temperature through the holding table 4. At the same time, the vapor-phase growth gas is introduced laterally into the reaction tube 1 from the vapor-phase growth gas introduction tube 2 and flows over the surface of the substrate 7 placed on the holding table 4 provided in the reaction tube 1. By this operation, the vapor growth gas flows in the reaction tube 1 in parallel with the surface of the substrate 7 and is thermally decomposed in a high temperature portion near the substrate 7 to deposit a reaction product on the surface of the substrate 7 to form a growth film.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかし、前記従来装置では成長膜が均一の厚さになら
ず、良好な成膜基板が得られない欠点があった。これは
気相成長ガス中の原料ガスが反応生成物となって基板7
面に次々に堆積し減少してもより上層の気相成長ガスか
らの原料ガスの補給が間に合わず、このため基板7面上
に流れる気相成長ガス中の原料ガスが流れに沿って減少
する濃度分布となり、この結果、基板7面の成長膜が上
流で厚く、下流で薄く形成されるためである。また、気
相成長ガスは基板7近傍の高温部で熱分解して堆積する
ので基板7の上流側にも堆積物8(以下、有害堆積物8
という)が堆積し、該有害堆積物8はその表面が剥離し
て気相成長ガスに同伴して基板7面上の成長膜に付着し
欠陥を生じさせる。そしてこれは有害堆積物8の量が多
い程増加する。そこで通常は気相成長処理をバッチ式で
繰り返しながら成長膜の欠陥率を調べ、該欠陥率が所定
以上の割合になったら気相成長処理を中断し反応管1内
を清掃し、前記有害堆積物8を除去しているが、前記従
来装置では有害堆積物の量が多いため頻繁な清掃が不可
欠である生産性が悪かった。
However, the conventional device has a drawback that the grown film does not have a uniform thickness and a good film formation substrate cannot be obtained. This is because the raw material gas in the vapor phase growth gas becomes a reaction product and the substrate 7
Even if the gas gradually grows on the surface, the supply of the source gas from the vapor-phase growth gas in the upper layer cannot be done in time, so that the source gas in the vapor-phase growth gas flowing on the surface of the substrate 7 decreases along the flow. This is because there is a concentration distribution, and as a result, the growth film on the surface of the substrate 7 is formed thicker on the upstream side and thinner on the downstream side. Further, since the vapor-phase growth gas is thermally decomposed and deposited in a high temperature portion near the substrate 7, a deposit 8 (hereinafter referred to as a harmful deposit 8) is also formed on the upstream side of the substrate 7.
That is, the surface of the harmful deposit 8 is peeled off and is accompanied by the vapor phase growth gas to adhere to the growth film on the surface of the substrate 7 to cause defects. And this increases as the amount of harmful deposits 8 increases. Therefore, normally, the defect rate of the grown film is checked while repeating the vapor phase growth process in batches, and when the defect rate exceeds a predetermined rate, the vapor phase growth process is interrupted and the inside of the reaction tube 1 is cleaned to remove the harmful deposition. Although the object 8 is removed, the conventional apparatus has a large amount of harmful deposits, and therefore frequent cleaning is indispensable, which is poor in productivity.

そこで、これらの不都合に対して基板を気相成長ガスの
流れ方向に対して傾けた状態で気相成長する方法が提案
されている。この方法によれば、基板面に形成される成
長膜の厚さを気相成長ガスの流れ方向に均一にすること
ができるが気相成長ガスは層流状態で流れるので中心部
の流速が速くなり気相成長ガスの流れと垂直な方向では
中心部が厚く、周辺部が薄くなり均一の厚さにはならな
い。また、前記の如く基板を傾けると、基板を自動的に
保持台上に移載するための基板搬送機構が複雑になる不
都合を新たに生ずる他、本方法によっても前記有害堆積
物は減少せず生産性は改善されない。
Therefore, a method of performing vapor phase growth in a state in which the substrate is inclined with respect to the flow direction of the vapor phase growth gas has been proposed against these disadvantages. According to this method, the thickness of the growth film formed on the substrate surface can be made uniform in the flow direction of the vapor growth gas, but since the vapor growth gas flows in a laminar state, the flow velocity at the center is high. In the direction perpendicular to the flow of the vapor deposition gas, the central portion is thick and the peripheral portion is thin, and the thickness is not uniform. In addition, if the substrate is tilted as described above, there is a new inconvenience that the substrate transfer mechanism for automatically transferring the substrate onto the holding table becomes complicated, and the harmful deposit is not reduced by this method. Productivity is not improved.

また、更に別の方法として、前記第3図の保持台4を水
平方向に回転する方法が提案されている。この方法によ
れば、成長膜は均一の厚さにできるものの、別途回転機
構を要し装置構成が複雑になるだけでなく、本方法によ
っても前記有害堆積物は減少せず生産性は改善されな
い。
As still another method, a method of horizontally rotating the holding table 4 shown in FIG. 3 has been proposed. According to this method, the growth film can be made to have a uniform thickness, but it requires a separate rotation mechanism to complicate the apparatus configuration, and this method does not reduce the harmful deposits nor improve the productivity. .

〔問題点を解決するための手段〕[Means for solving problems]

本発明は前記不都合に鑑みてなされたもので、均一な成
長膜を形成し得ると共に、基板より上流での前記有害堆
積物の量を減少して生産性を向上させた気相成長装置を
提供することを目的とし、その特徴とするところは、反
応管内を横方向に流れる気相成長ガスを、反応管内に設
けた保持台上に載置した基板面上に流して、該基板面に
成長膜を形成する気相成長装置において、反応管内の基
板より上流部分を、基板面と平行に配設した仕切板によ
り上部流路と下部基板面側流路とに区画して上下平行流
路を形成し、上部流路に気相成長ガス導入管を、下部基
板面側流路に介在ガス導入管をそれぞれ連設したことに
ある。
The present invention has been made in view of the above-mentioned inconvenience, and provides a vapor phase growth apparatus capable of forming a uniform growth film and reducing the amount of the harmful deposit upstream of the substrate to improve the productivity. The feature is that the vapor phase growth gas flowing in the reaction tube in the lateral direction is flown onto the substrate surface placed on the holding table provided in the reaction tube to grow on the substrate surface. In a vapor phase growth apparatus for forming a film, a part in the reaction tube upstream of the substrate is divided into an upper channel and a lower substrate surface side channel by a partition plate arranged in parallel with the substrate surface to form a vertical parallel channel. That is, the vapor phase growth gas introduction pipe is formed in the upper flow path, and the intervening gas introduction pipe is connected in the lower substrate surface side flow path.

〔実施例〕〔Example〕

以下、本発明の一実施例を図面を用いて説明する。 An embodiment of the present invention will be described below with reference to the drawings.

第1図は本実施例に係る気相成長装置の断面図、第2図
は第1図のII−II断面図で、図中前記第3図と同一構成
部分には同一記号を付してある。
FIG. 1 is a sectional view of a vapor phase growth apparatus according to this embodiment, and FIG. 2 is a sectional view taken along line II-II of FIG. 1, in which the same components as those in FIG. is there.

図において、10は反応管1内の基板7より上流部分に基
板7面と平行に配設した仕切板で、該仕切板10により反
応管1内の基板7より上流部分を、上部流路9aと下部基
板面側流路9bとに区画して上下平行流路9を形成し、上
部流路9aに気相成長ガス導入管11を、下部基板面側流路
9bに介在ガス導入管12をそれぞれ連設する。仕切板10
は、基板7に達しない長さの板状物で、その基板側端部
10aは、第2図の如く、長手方向に沿って中央部が膨出
するよう例えば半円状に膨出した形状に形成されてい
る。
In the figure, 10 is a partition plate arranged in the reaction tube 1 upstream of the substrate 7 in parallel with the surface of the substrate 7. And a lower substrate surface side channel 9b to form an upper and lower parallel channel 9, and an upper growth channel 9a is provided with a vapor growth gas introducing pipe 11 and a lower substrate surface side channel 9b.
Intervening gas introducing pipes 12 are connected to 9b, respectively. Partition plate 10
Is a plate-like object having a length that does not reach the substrate 7, and its end on the substrate side
As shown in FIG. 2, the reference numeral 10a is formed in a shape that bulges out, for example, in a semicircular shape so that the central portion bulges out along the longitudinal direction.

前記の如く構成された本実施例装置は、基板7を所定の
温度に保持すると共に、介在ガス導入管11に介在ガス
を、気相成長ガス導入管12に気相成長ガスをそれぞれ導
入して使用する。この場合、介在ガスとしては稀釈ガス
または、これに少量の揮発抑制ガスを添加したものを用
いる。揮発抑制ガスとは基板7を構成する物質のうち熱
により揮発する成分の揮発を抑制するためのガスであ
り、例えばGaAs基板の場合はAsの揮発を防止するためAs
H3を抑制ガスとして少量流す。
The apparatus of the present embodiment configured as described above holds the substrate 7 at a predetermined temperature, introduces the intervening gas into the intervening gas introduction pipe 11 and introduces the vapor growth gas into the vapor growth gas introduction pipe 12, respectively. use. In this case, as the intervening gas, a diluting gas or a gas in which a small amount of a volatilization suppressing gas is added is used. The volatilization suppressing gas is a gas for suppressing volatilization of a component of the substrate 7 which is volatilized by heat. For example, in the case of a GaAs substrate, As is used to prevent volatilization of As.
A small amount of H 3 is used as a suppressing gas.

前記の如く、気相成長ガスと介在ガスは、上下平行流路
9の上部流路9aと下部基板面側流路9bとを別々に相互に
平行に流れ、仕切板10の基板側端部10aを過ぎた後は相
互に拡散しながら基板7に向って流れ、このため介在ガ
スは原料ガス濃度に徐々に高めながら基板7面に接近す
るが、基板7面通過時は、前記相互拡散作用により気相
成長ガス中の原料ガスが引き続き介在ガス中に入ってく
ると共に、該介在ガス中の原料ガスは反応生成物となっ
て次々に基板7面に堆積する。従って介在ガス,気相成
長ガスの流速,気相成長ガス中の原料ガス濃度を適宜調
節することにより、気相成長ガスから介在ガスに流入す
る原料ガス量と基板7面への堆積により介在ガスから消
失する原料ガス量とを単位時間当りでバランスすること
ができ、これによって基板7面通過時の介在ガス中の原
料ガスを流れ方向に均一な濃度分布として均一な膜厚の
成長膜を形成でき良好な成膜基板を得ることができる。
As described above, the vapor-phase growth gas and the intervening gas separately flow in parallel in the upper channel 9a and the lower substrate surface side channel 9b of the upper and lower parallel channel 9, and the substrate side end portion 10a of the partition plate 10 is separated. After passing through, the interstitial gas flows toward the substrate 7 while diffusing with each other. Therefore, the intervening gas approaches the surface of the substrate 7 while gradually increasing the concentration of the raw material gas. The raw material gas in the vapor phase growth gas continuously enters the intervening gas, and the raw material gas in the intervening gas becomes a reaction product and is successively deposited on the surface of the substrate 7. Therefore, by appropriately adjusting the intervening gas, the flow velocity of the vapor growth gas, and the concentration of the raw material gas in the vapor growth gas, the amount of the raw material gas flowing from the vapor growth gas into the interposing gas and the interposition gas due to the deposition on the surface of the substrate 7 It is possible to balance the amount of the raw material gas disappeared per unit time per unit time, thereby forming a growth film having a uniform film thickness with a uniform concentration distribution of the raw material gas in the intervening gas when passing through the surface of the substrate 7 As a result, a good film formation substrate can be obtained.

また、前記介在ガスはその原料ガス濃度が気相成長ガス
より薄い状態で、基板側端部10aから基板7面上を流れ
るので、気相成長ガスがそのまま接触する従来装置に比
べ有害堆積物8の量が減少し、これに伴って清掃回数も
減少するので生産性が向上する。
Further, the intervening gas flows from the substrate-side end portion 10a onto the surface of the substrate 7 in a state where the source gas concentration thereof is lower than that of the vapor phase growth gas. The number of cleanings is reduced and the number of cleanings is also reduced, which improves productivity.

以上の如く、仕切板10を設けることにより成膜膜の膜厚
を流れ方向に均一化できるが、仕切板10の基板側端部10
aを第2図の半円形状の如く仕切板10の長手方向に沿っ
て膨出する形状に形成すればより均一な膜厚とすること
ができる。即ち、通常、介在ガスは反応管1内を層流で
流すので流速分布が中心部で速く、周辺部で遅くなり、
このため成長膜が流速の速い部分では厚く,遅い部分で
は薄くなるが、前記端部10aの半円形状により介在ガス
と気相成長ガスの相互拡散の開始を中心部が周辺部より
遅れるよう調整でき、これにより前記基板側端部10a通
過後の介在ガス中の原料ガスの濃度分布を第2図13a,13
b,13cの如くすると、介在ガスの流速分布は破線表示し
た14の如くなるので基板7面上における介在ガスの流速
が速い部分では原料ガスの濃度を薄く、また、介在ガス
の流速が遅い部分では原料ガスの濃度を濃くすることが
でき、成長膜を介在ガスの流れ方向に対し垂直な方向で
均一な厚さとすることができ、前記流れ方向の均一化と
併せほぼ全面を均一にでき極めて良好な成膜基板を得る
ことができる。なお、前記実施例では一枚の基板を処理
する装置の場合で説明したが、複数枚の基板を同時に処
理する装置にも応用できることは言う迄もない。
As described above, by providing the partition plate 10, the film thickness of the deposited film can be made uniform in the flow direction.
A more uniform film thickness can be obtained by forming a into a shape that bulges along the longitudinal direction of the partition plate 10 as in the semicircular shape in FIG. That is, since the intervening gas normally flows in a laminar flow in the reaction tube 1, the flow velocity distribution is fast in the central part and slow in the peripheral part,
For this reason, the growth film becomes thicker in the portion where the flow velocity is faster and thinner in the portion where the flow velocity is slower, but the semicircular shape of the end portion 10a is adjusted so that the start of the interdiffusion of the intervening gas and the vapor growth gas is delayed in the central portion than in the peripheral portion. As a result, the concentration distribution of the raw material gas in the intervening gas after passing through the substrate side end portion 10a is shown in FIG.
If b and 13c are used, the flow velocity distribution of the intervening gas becomes as shown by the broken line 14, so that the concentration of the source gas is thin in the part where the flow velocity of the intervening gas is fast on the surface of the substrate 7 and the part where the flow velocity of the intervening gas is slow. The concentration of the raw material gas can be made high, and the growth film can have a uniform thickness in the direction perpendicular to the flow direction of the intervening gas. Together with the uniformization of the flow direction, almost the entire surface can be made uniform. A good film formation substrate can be obtained. It should be noted that the above embodiment has been described in the case of an apparatus for processing one substrate, but it goes without saying that it can be applied to an apparatus for simultaneously processing a plurality of substrates.

〔発明の効果〕〔The invention's effect〕

本発明装置は、以上の如く、気相成長ガスが横方向に流
れる反応管内の基板より上流部分を、基板面と平行な仕
切板により上部流路と下部基板面側流路とに区画して上
下平行流路を形成し、上部流路に気相成長ガス導入管
を、下部基板面側流路に介在ガス導入管をそれぞれ連設
したので、 (1)上下平行流路の上部流路と下部基板面側流路とを
別々に相互に平行に流れる気相成長ガスと介在ガスが、
仕切板の基板側端部を過ぎた後は相互に拡散しながら基
板に向って流れるため、介在ガスは原料ガス濃度を徐々
に高めながら基板面に接近し、基板面通過時に介在ガス
中の原料ガスは反応生成物となって次々に基板面に堆積
するから、気相成長ガスのみによる気相成長に比べて、
基板面に形成する成長膜の厚さを気相成長ガスの流れ方
向に対して均一にすることができ、基板を保持台上に水
平に載置したまま気相成長を実施できるので、基板を傾
ける従来法に比べ基板搬送機構が簡単になり、また保持
台を回転する従来法に比べても保持台を回転する機構が
不要なので装置構成が簡素になる。
As described above, the apparatus of the present invention divides the upstream portion of the substrate in the reaction tube in which the vapor growth gas flows in the lateral direction into the upper channel and the lower substrate surface side channel by the partition plate parallel to the substrate surface. Since the upper and lower parallel flow paths are formed, the vapor phase growth gas introduction pipe is connected to the upper flow path, and the intervening gas introduction pipe is connected to the lower substrate surface side flow path, respectively. The vapor growth gas and the intervening gas that flow separately and in parallel with the lower substrate surface side flow path,
After passing through the end of the partition plate on the substrate side, they flow toward the substrate while diffusing each other, so that the intervening gas approaches the substrate surface while gradually increasing the concentration of the raw material gas, and the raw material in the intervening gas when passing through the substrate surface. Since gas becomes a reaction product and is deposited on the substrate surface one after another, compared with vapor phase growth using only vapor phase growth gas,
The thickness of the growth film formed on the surface of the substrate can be made uniform with respect to the flow direction of the vapor phase growth gas, and the vapor phase growth can be performed while the substrate is placed horizontally on the holding table. The substrate transfer mechanism is simpler than the conventional method of tilting, and the mechanism for rotating the holding table is not necessary compared to the conventional method of rotating the holding table, so that the apparatus configuration is simplified.

(2)また、介在ガスはその原料ガス濃度が気相成長ガ
スより薄い状態で基板面上を流れるから、気相成長時に
おける基板上流側での有害堆積物を従来より減少するこ
とができ、清掃回数が減少し、生産性が向上し、経済的
である。
(2) Further, since the intervening gas flows on the substrate surface in a state where the source gas concentration thereof is thinner than that of the vapor phase growth gas, it is possible to reduce harmful deposits on the upstream side of the substrate during vapor phase growth as compared with the conventional case. Cleaning frequency is reduced, productivity is improved, and it is economical.

(3)さらに、仕切板の基板側端部を長手方向に沿って
中央部が膨出する形状に形成すれば、気相成長ガスの流
れと垂直な方向における成長膜の厚さを均一化でき、前
記(1)(2)の効果と併せ、略全面に亘って成長膜の
厚さを均一化することができる。そしてこれは、保持台
を回転させて全面を均一な膜厚とする従来法に比べ保持
台回転機構を要せずして実現できる点が特長的である。
(3) Further, if the end portion of the partition plate on the substrate side is formed so that the central portion bulges along the longitudinal direction, the thickness of the growth film in the direction perpendicular to the flow of the vapor growth gas can be made uniform. In addition to the effects of (1) and (2) above, the thickness of the growth film can be made uniform over almost the entire surface. This is characterized by the fact that it can be realized without the need for a holder rotating mechanism, as compared with the conventional method in which the holder is rotated to obtain a uniform film thickness on the entire surface.

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

第1図は本発明の気相成長装置の一実施例を示す断面
図、第2図は第1図のII−II断面図、第3図は従来の気
相成長装置の断面図である。 1……反応管、3……排出管、4……保持台、5……フ
ローチャンネル、5……FRコイル、7……基板、8……
有害堆積物、9……上下平行流路、9a……上部流路、9b
……下部基板面側流路、10……仕切板、11……気相成長
ガス導入管、12……介在ガス導入管
FIG. 1 is a sectional view showing an embodiment of the vapor phase growth apparatus of the present invention, FIG. 2 is a sectional view taken along line II-II of FIG. 1, and FIG. 3 is a sectional view of a conventional vapor phase growth apparatus. 1 ... Reaction tube, 3 ... Discharge tube, 4 ... Holding stand, 5 ... Flow channel, 5 ... FR coil, 7 ... Substrate, 8 ...
Hazardous sediments, 9 …… Upper and lower parallel flow paths, 9a …… Upper flow path, 9b
...... Lower substrate surface side flow path, 10 ...... Partition plate, 11 …… Gas phase growth gas introduction pipe, 12 …… Interposed gas introduction pipe

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】反応管内を横方向に流れる気相成長ガス
を、反応管内に設けた保持台上に載置した基板面上に流
して、該基板面に成長膜を形成する気相成長装置におい
て、反応管内の基板より上流部分を、基板面と平行に配
設した仕切板により上部流路と下部基板面側流路とに区
画して上下平行流路を形成し、上部流路に気相成長ガス
導入管を、下部基板面側流路に介在ガス導入管をそれぞ
れ連設したことを特徴とする気相成長装置。
1. A vapor phase growth apparatus for forming a growth film on a surface of a substrate placed on a holding table provided in the reaction tube by flowing a vapor growth gas flowing laterally in the reaction tube. In the above, the upstream portion of the reaction tube from the substrate is divided into an upper channel and a lower substrate surface side channel by a partition plate arranged parallel to the substrate surface to form an upper and lower parallel channel, and the upper channel is filled with air. A vapor phase growth apparatus comprising a phase growth gas introduction pipe and an intervening gas introduction pipe connected to a lower substrate surface side flow path.
【請求項2】前記仕切板が基板側端部で長手方向に沿っ
て中央部が膨出する形状に形成されてなることを特徴と
する特許請求の範囲第1項に記載の気相成長装置。
2. The vapor phase growth apparatus according to claim 1, wherein the partition plate is formed in such a shape that the central portion bulges along the longitudinal direction at the substrate side end portion. .
JP62099147A 1987-04-22 1987-04-22 Vapor phase growth equipment Expired - Fee Related JPH0727868B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62099147A JPH0727868B2 (en) 1987-04-22 1987-04-22 Vapor phase growth equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62099147A JPH0727868B2 (en) 1987-04-22 1987-04-22 Vapor phase growth equipment

Publications (2)

Publication Number Publication Date
JPS63263718A JPS63263718A (en) 1988-10-31
JPH0727868B2 true JPH0727868B2 (en) 1995-03-29

Family

ID=14239581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62099147A Expired - Fee Related JPH0727868B2 (en) 1987-04-22 1987-04-22 Vapor phase growth equipment

Country Status (1)

Country Link
JP (1) JPH0727868B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997036320A1 (en) * 1996-03-22 1997-10-02 Nippon Sanso Corporation Vapor phase growth apparatus and vapor phase growth method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011192768A (en) * 2010-03-15 2011-09-29 Mitsui Eng & Shipbuild Co Ltd Atomic layer deposition device and atomic layer deposition method

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS52143599A (en) * 1976-05-24 1977-11-30 Nippon Eaatetsuku Kk Device for removing chemical dusts for use in wrapping machine

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1997036320A1 (en) * 1996-03-22 1997-10-02 Nippon Sanso Corporation Vapor phase growth apparatus and vapor phase growth method

Also Published As

Publication number Publication date
JPS63263718A (en) 1988-10-31

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