JPH04157716A - Vapor growth apparatus - Google Patents

Vapor growth apparatus

Info

Publication number
JPH04157716A
JPH04157716A JP28283490A JP28283490A JPH04157716A JP H04157716 A JPH04157716 A JP H04157716A JP 28283490 A JP28283490 A JP 28283490A JP 28283490 A JP28283490 A JP 28283490A JP H04157716 A JPH04157716 A JP H04157716A
Authority
JP
Japan
Prior art keywords
outer tube
reaction
tube
material gas
growth apparatus
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
JP28283490A
Other languages
Japanese (ja)
Inventor
Akinori Shimizu
清水 明徳
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 JP28283490A priority Critical patent/JPH04157716A/en
Publication of JPH04157716A publication Critical patent/JPH04157716A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To reduce a deposit on an evacuation pipe and to enhance the operation rate of a vapor growth apparatus by a method wherein a protrusion part is formed at least either on the inner surface of an outer tube or on the outer surface of an inner tube. CONSTITUTION:At this vapor growth apparatus, its surface area is increased to about eight times by means of protrusion parts 15 formed on the surface of an outer tube 2. As a result, when an unreacted raw-material gas and a reaction by-product fall between an inner tube 4 and the outer tube 2, a deposit by the vapor-phase reaction of the raw-material gas and a deposit 14 by the reaction by-product are easily produced on the surface of the outer tube 2, and the raw-material gas and the reaction by-product are consumed much. As a result, the amount of the raw-material gas and the reaction by-product which flow into an evacuation pipe 11 becomes extremely small, and the deposit there is reduced sharply. As a result, the periodic cleaning frequency of the vapor growth apparatus is reduced sharply and its operation rate is enhanced sharply.

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、特に半導体ウェハー表面
上に薄膜を形成する縦型減圧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 reduced pressure vapor phase growth apparatus for forming a thin film on the surface of a semiconductor wafer.

〔従来の技術〕[Conventional technology]

半導体ウェハー表面上に薄膜を形成するのに縦型減圧気
相成長装置が近年多く用いられるようになってきている
。従来の縦型減圧気相成長装置の一例の断面図を第3図
に示す。
In recent years, vertical low pressure vapor phase growth apparatuses have been increasingly used to form thin films on the surfaces of semiconductor wafers. A cross-sectional view of an example of a conventional vertical reduced pressure vapor phase growth apparatus is shown in FIG.

気相成長反応室41の外側は、上端が閉じられた円筒形
の石英製の外管42およびそれを支持するステンレス製
台43より成る。反応室41内部 ゛には、両端の開か
れた円筒型の石英製の内管44がこのステンレス敷台4
3上に配され、さらにその内部には石英製ボート45が
配され、半導体ウェハー46が石英製ボート45上に水
平に配される。石英製ボート45は、上下動可能なステ
ンレス製ハツチ47に支持されており、気相成長中はこ
のステンレス製ハツチ47はステンレス製台43に密着
され、反応室内は密べいされる。また、外管42の外部
にはヒーター48が配置され、反応室41内部が加熱さ
れる。原料ガスを供給するガス導入管49が反応室41
の外部より内管44内部の下部へ通じ、また外管42の
側面下部には排気口50が設けられ、ゲートバルブ52
を有し真空ポンプ53へ通じる排気配管51が接続され
ている。
The outside of the vapor phase growth reaction chamber 41 consists of a cylindrical quartz outer tube 42 with a closed upper end and a stainless steel stand 43 that supports it. Inside the reaction chamber 41, a cylindrical quartz inner tube 44 with both ends open is connected to the stainless steel base 4.
A quartz boat 45 is disposed inside the quartz boat 45, and a semiconductor wafer 46 is disposed horizontally on the quartz boat 45. The quartz boat 45 is supported by a stainless steel hatch 47 that can be moved up and down, and during vapor phase growth, the stainless steel hatch 47 is brought into close contact with the stainless steel stand 43, and the reaction chamber is sealed tightly. Further, a heater 48 is arranged outside the outer tube 42 to heat the inside of the reaction chamber 41. A gas introduction pipe 49 for supplying raw material gas is connected to the reaction chamber 41.
An exhaust port 50 is provided at the lower side of the outer tube 42 to communicate with the lower part of the inner tube 44 from the outside.
An exhaust pipe 51 is connected thereto and leads to a vacuum pump 53.

気相成長中は真空ポンプ53により反応室41内が減圧
にされ、原料ガスがガス導入管49より内管44内部へ
導入され、矢印に従って内管44内を上昇しながら気相
反応により半導体ウェハー46表面に薄膜が形成される
。未反応の原料ガスや気相反応により生じた副生成ガス
等は、内管44と外管42の間を下降し、排気配管51
を通じて真空ポンプ53で排気される。
During vapor phase growth, the inside of the reaction chamber 41 is reduced in pressure by the vacuum pump 53, and the raw material gas is introduced into the inner tube 44 through the gas introduction tube 49, and as it ascends inside the inner tube 44 according to the arrow, the semiconductor wafer is heated through a vapor phase reaction. A thin film is formed on the surface of 46. Unreacted raw material gas and by-product gas generated by the gas phase reaction descend between the inner pipe 44 and the outer pipe 42 and reach the exhaust pipe 51.
The air is evacuated by a vacuum pump 53 through the air.

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

一般にこの種の縦型気相成長装置による気相成長では、
原料ガスが半導体ウェハーの表面上への気相成長にすべ
て消費されるわけではなく、多量の未反応の原料ガスや
、気相成長反応による副生成物が内管と外管の間に流れ
こむ。従来この内管の外壁表面および外管の内壁表面は
平坦であり凹凸がないため、外管と内管の間での原料ガ
スの気相成長反応による堆積や反応副生成物の堆積はほ
とんどおこらない、そのため、多量の未反応の原料ガス
や副生成物等が排気配管内に流れこみ、第3図に示すよ
うに、堆積物54が多く発生し、排気配管をつまらせて
しまうという問題点があった。
Generally, in vapor phase growth using this type of vertical vapor phase growth apparatus,
Not all of the raw material gas is consumed for vapor phase growth on the surface of the semiconductor wafer, and a large amount of unreacted raw material gas and byproducts from the vapor phase growth reaction flow between the inner and outer tubes. . Conventionally, the outer wall surface of the inner tube and the inner wall surface of the outer tube are flat and free of irregularities, so deposition due to the vapor growth reaction of the raw material gas and deposition of reaction byproducts between the outer tube and the inner tube rarely occur. Therefore, a large amount of unreacted raw material gas, by-products, etc. flow into the exhaust pipe, and as shown in FIG. 3, a large amount of deposits 54 are generated, which causes the exhaust pipe to become clogged. was there.

〔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、反応室の外側が上端の閉じら
れた円筒形の外管とこの外管を支持する台より構成され
、前記外管内に両端が開かれた円筒形の内管が前記台上
に配され、前記内管の内部に原料ガスを導入するガス導
入管が設けられ、前記外管の一部にガス排気口を有し、
前記内管の内部に配置された半導体基板上に膜を形成す
る気相成長装置において、前記外管の内表面もしくは前
記内管の外表面の少くとも一方に凸部を設けたものであ
る。
The vapor phase growth apparatus of the present invention consists of a cylindrical outer tube with a closed upper end on the outside of the reaction chamber and a stand supporting the outer tube, and a cylindrical inner tube with both ends open inside the outer tube. is arranged on the table, a gas introduction pipe for introducing raw material gas into the inside of the inner pipe is provided, and a part of the outer pipe has a gas exhaust port,
In the vapor phase growth apparatus for forming a film on a semiconductor substrate placed inside the inner tube, a convex portion is provided on at least one of the inner surface of the outer tube or the outer surface of the inner tube.

〔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図は本発明の第1の実施例の断面図である。FIG. 1 is a sectional view of a first embodiment of the invention.

第1図に示すように、反応室1の外側は、上端が閉じら
れた円筒形の石英製の外管2とこの外管2をのせるステ
ンレス製台3より構成されている。外管2は、例えば内
径が50 cm 、側面部分の高さが100cmであり
、その内表面には、側面下部に設けられた内径数1の排
気口10の部分を除き幅が0.5cm高さが11cmの
凸部15がリング状に、11間隔で60個設けられてい
る。そしてこの反応室1内に両端の開かれた外径241
.高さ100C!lの円筒型の石英製の内管4がステン
レス裏白3上に配置されている。
As shown in FIG. 1, the outside of the reaction chamber 1 is composed of a cylindrical outer tube 2 made of quartz with a closed upper end and a stainless steel stand 3 on which the outer tube 2 is placed. The outer tube 2 has, for example, an inner diameter of 50 cm and a height of 100 cm at the side surface, and the inner surface has a width of 0.5 cm and a height except for the exhaust port 10 with an inner diameter of 1 provided at the bottom of the side surface. Sixty convex portions 15 each having a length of 11 cm are provided in a ring shape at 11 intervals. Inside this reaction chamber 1, an outer diameter 241 is opened at both ends.
.. Height 100C! A cylindrical inner tube 4 made of quartz is placed on a stainless steel backing 3.

外管2と内管4の間の表面積を考える。外管2の側面内
表面と内管4の側面外表面の表面積の和は、排気口を無
視すれば、凸部15がない場合は23248calであ
るが、凸部15が設けられた場合は凸部1つにつき表面
積が2695.5C11!増加するなめ、凸部全体では
161729ctd増加して187977−となる。す
なわちこの凸部により表面積が約8倍となる。
Consider the surface area between the outer tube 2 and the inner tube 4. The sum of the surface areas of the inner surface of the side surface of the outer tube 2 and the outer surface of the side surface of the inner tube 4 is 23248 cal if there is no convex part 15, ignoring the exhaust port, but if the convex part 15 is provided, The surface area per part is 2695.5C11! Due to the increase, the entire convex portion increases by 161,729ctd to 187,977-. In other words, this convex portion increases the surface area by about eight times.

内管4の内部には石英製ボート5が配置され、半導体ウ
ェハー6が石英製ボート5上に配置される。この石英製
ボート5は上下動可能なステンレス製ハツチ7に支持さ
れており、気相成長中はこのステンレス製ハツチ7はス
テンレス製台3に密着され、反応室1内は密へいされる
。また外管2の外部にはヒーター8が配され、反応室1
の内部が加熱される。原料ガスを供給するガス導入管9
が反応室1の外部より内管4内部の下部へ通じている。
A quartz boat 5 is arranged inside the inner tube 4, and a semiconductor wafer 6 is arranged on the quartz boat 5. This quartz boat 5 is supported by a stainless steel hatch 7 that can be moved up and down, and during vapor phase growth, this stainless steel hatch 7 is closely attached to the stainless steel stand 3, so that the inside of the reaction chamber 1 is sealed tightly. Further, a heater 8 is arranged outside the outer tube 2, and a heater 8 is arranged outside the reaction chamber 1.
The inside of the is heated. Gas introduction pipe 9 for supplying raw material gas
is connected from the outside of the reaction chamber 1 to the lower part of the inside of the inner tube 4.

また外管2の側面下部の排気口1oに排気配管11が接
続されている。排気配管工1はゲートバルブ12を有し
真空ポンプ13に接続されている。
Further, an exhaust pipe 11 is connected to an exhaust port 1o at the lower side of the outer tube 2. The exhaust plumber 1 has a gate valve 12 and is connected to a vacuum pump 13.

気相成長の際は反応室1内が真空ポンプ13により減圧
にされ、ガス導入管9より原料ガスが内管4内に導入さ
れ矢印に従って内管4内を上昇にしながら、半導体ウェ
ハー6表面上に気相反応により薄膜を堆積する。未反応
の原料ガスや気相反応により生じたガス状の反応副生成
物は、内管4と外管2との間を下降し、排気配管11を
通じて真空ポンプ13で排気される。
During vapor phase growth, the inside of the reaction chamber 1 is reduced in pressure by the vacuum pump 13, and the raw material gas is introduced into the inner tube 4 from the gas introduction tube 9, and as it moves upward in the inner tube 4 according to the arrow, it is deposited on the surface of the semiconductor wafer 6. A thin film is deposited by a gas phase reaction. Unreacted raw material gas and gaseous reaction by-products generated by the gas phase reaction descend between the inner tube 4 and the outer tube 2 and are exhausted by the vacuum pump 13 through the exhaust pipe 11.

本草1の実施例では、外管2表面に設けられた凸部15
により表面積が約8倍となっている。ため、未反応の原
料ガスや反応副生成物が、内管4と外管2の間を下降す
る際、外管2の表面上で原料ガスの気相反応による堆積
や、反応副生成物の堆積14が生じやすくなり、そこで
原料ガスや反応副生成物の多くが消費されるようになる
。そのため、排気配管11へ流れこむ原料ガスや反応副
生成物の量はきわめて少くなり、そこでの堆積は大幅に
減少する。
In the embodiment of the herb 1, the convex portion 15 provided on the surface of the outer tube 2
The surface area is approximately 8 times larger. Therefore, when the unreacted raw material gas and reaction by-products descend between the inner tube 4 and the outer tube 2, they are deposited on the surface of the outer tube 2 due to the gas phase reaction of the raw material gas, and the reaction by-products are deposited on the surface of the outer tube 2. Deposition 14 tends to occur, and much of the raw material gas and reaction by-products are consumed there. Therefore, the amount of raw material gas and reaction by-products flowing into the exhaust pipe 11 becomes extremely small, and the amount of deposition there is significantly reduced.

例えば、アンモニア(NH,il)ジクロルシラン(S
iC12H2>を原料ガスとして窒化けい素膜(Si3
N4)を形成する場合、本実施例によれば、内管4の内
部で未反応であった原料ガスは、内管4と外管2の間を
下降する際、外管2の凸部15による表面積の増大のた
め、その表面上に窒化けい素を堆積する気相反応が起る
ため、未反応の原料ガスの多くがそこで消費され、排気
配管へ流れこむ量は大幅に減少する。
For example, ammonia (NH,il) dichlorosilane (S
A silicon nitride film (Si3
According to this embodiment, when forming N4), the unreacted raw material gas inside the inner tube 4 passes through the convex portion 15 of the outer tube 2 when descending between the inner tube 4 and the outer tube 2. Due to the increase in surface area, a gas phase reaction occurs that deposits silicon nitride on the surface, so much of the unreacted raw material gas is consumed there, and the amount flowing into the exhaust pipe is greatly reduced.

またこの気相反応では、副生成物として塩化アンモニウ
ム(NH4CJ)を生じるが、これも多くは、内管4と
外管2の間に堆積されるため、排気管11内に堆積する
量を大幅に減らすことができる。この場合、外管2の表
面積を8倍にすることにより、排気配管11内に堆積す
る量は従来に比較して115程度になる。そのため本気
相成長装置の定期清掃頻度が大幅に低減し、稼働率が大
幅に向上するという長所がある。 第2図は本発明の第
2の実施例の断面図である。
In addition, in this gas phase reaction, ammonium chloride (NH4CJ) is produced as a byproduct, but since most of this is deposited between the inner pipe 4 and the outer pipe 2, the amount deposited in the exhaust pipe 11 can be greatly reduced. can be reduced to In this case, by increasing the surface area of the outer tube 2 by eight times, the amount deposited in the exhaust pipe 11 will be about 115 times that of the conventional case. This has the advantage that the frequency of periodic cleaning of the serious vapor phase growth apparatus is greatly reduced, and the operating rate is greatly improved. FIG. 2 is a sectional view of a second embodiment of the invention.

本草2の実施例では、石英製の外管22の内壁表面およ
び石英製の内管24の外壁表面の双方に凸部35を設け
た場合である。内径50cIlの外管22の内表面に、
厚さ0.5CII長さ60m1の凸部35がリング状に
1cm間隔で60個、外径240Iの内管24の外表面
には厚さ0.5CII長さ6C1lの凸部35がリング
状に1cm間隔で60個設けられている。これにより表
面積は凸部35がない場合の23248−に比べ190
632adとなり、約8.2倍に増加する。
In the example of Honso 2, the convex portions 35 are provided on both the inner wall surface of the outer tube 22 made of quartz and the outer wall surface of the inner tube 24 made of quartz. On the inner surface of the outer tube 22 with an inner diameter of 50 cIl,
There are 60 ring-shaped protrusions 35 with a thickness of 0.5 CII and a length of 60 m1, spaced at 1 cm intervals, and a ring-shaped protrusion 35 with a thickness of 0.5 CII and a length of 6 C1 l on the outer surface of the inner tube 24 with an outer diameter of 240 I. There are 60 pieces arranged at 1cm intervals. As a result, the surface area is 190 mm compared to 23248 mm without the convex portion 35.
632ad, an increase of approximately 8.2 times.

本草2の実施例の場合、ガスが外管22と内管24の間
を下降する除草1の実施例に比べ、よりガス分子が外管
22と内管24の表面に当たりやすくなり、更に凸部に
よりガスの流れに乱れを生じやすくなるため、外管22
と内管24の間での堆積がより生じやすくなる。そのた
め、排気配管31に堆積する量を更に減少させることが
できる。
In the case of Example 2, gas molecules are more likely to hit the surfaces of the outer tube 22 and inner tube 24 than in the example of Weeding 1, in which the gas descends between the outer tube 22 and the inner tube 24. This tends to cause turbulence in the gas flow, so the outer tube 22
Accumulation is more likely to occur between the inner tube 24 and the inner tube 24. Therefore, the amount deposited on the exhaust pipe 31 can be further reduced.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、気相成長装置において、
石英製外管の内壁表面もしくは石英製内管の外壁表面の
少くとも一方に凸部を設けることにより、外管と内管の
間に、そこを通過する未反応の原料ガスの気相反応によ
る堆積や気相反応副生成物の堆積を効果的に生じさせる
ことができる。そのため排気配管での堆積物を大幅に減
らすことができるため、気相成長装置の稼働率を大幅に
向上させることができるという効果がある。
As explained above, the present invention provides a vapor phase growth apparatus including:
By providing a convex portion on at least one of the inner wall surface of the quartz outer tube or the outer wall surface of the quartz inner tube, a convex portion is provided between the outer tube and the inner tube to prevent gas phase reaction of unreacted raw material gas passing therethrough. Deposition and deposition of gas phase reaction by-products can be effectively caused. Therefore, the amount of deposits in the exhaust pipe can be significantly reduced, resulting in the effect that the operating rate of the vapor phase growth apparatus can be significantly improved.

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

第1図及び第2図は本発明の第1及び第2の実施例の断
面図、第3図は従来の気相成長装置の一例の断面図であ
る。 1.21.41・・・反応室、2,22.42・・・石
英製外管、3,23.43・・・ステンレス製台、4.
24.44・・・石英製内管、5,25.45・・・石
英製ボート、6,26.46・・・半導体ウェハー、7
.27.47・・・ステンレス製ハツチ、8゜28.4
8・・・ヒーター、9,29.49・・・ガス導入管、
10.30.50・・・排気口、11.31゜51・・
・排気配管、12,32.52・・・ゲートバルブ、1
3.33.53・・・真空ポンプ、54・・・堆積物、
15.35・・・凸部。
1 and 2 are cross-sectional views of first and second embodiments of the present invention, and FIG. 3 is a cross-sectional view of an example of a conventional vapor phase growth apparatus. 1.21.41...Reaction chamber, 2,22.42...Quartz outer tube, 3,23.43...Stainless steel stand, 4.
24.44... Quartz inner tube, 5, 25.45... Quartz boat, 6, 26.46... Semiconductor wafer, 7
.. 27.47...Stainless steel hatch, 8°28.4
8...Heater, 9,29.49...Gas introduction pipe,
10.30.50...Exhaust port, 11.31°51...
・Exhaust piping, 12, 32.52... Gate valve, 1
3.33.53...Vacuum pump, 54...Deposit,
15.35...Protrusion.

Claims (1)

【特許請求の範囲】[Claims]  反応室の外側が上端の閉じられた円筒形の外管とこの
外管を支持する台より構成され、前記外管内に両端が開
かれた円筒形の内管が前記台上に配され、前記内管の内
部に原料ガスを導入するガス導入管が設けられ、前記外
管の一部にガス排気口を有し、前記内管の内部に配置さ
れた半導体基板上に膜を形成する気相成長装置において
、前記外管の内表面もしくは前記内管の外表面の少くと
も一方に凸部を設けたことを特徴とする気相成長装置。
The outside of the reaction chamber is composed of a cylindrical outer tube with a closed upper end and a stand supporting this outer tube, a cylindrical inner tube with both ends open inside the outer tube is placed on the stand, and the A gas introduction pipe for introducing raw material gas into the inner pipe is provided, a gas exhaust port is provided in a part of the outer pipe, and a gas phase is provided to form a film on a semiconductor substrate disposed inside the inner pipe. A vapor phase growth apparatus characterized in that a convex portion is provided on at least one of the inner surface of the outer tube or the outer surface of the inner tube.
JP28283490A 1990-10-19 1990-10-19 Vapor growth apparatus Pending JPH04157716A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28283490A JPH04157716A (en) 1990-10-19 1990-10-19 Vapor growth apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28283490A JPH04157716A (en) 1990-10-19 1990-10-19 Vapor growth apparatus

Publications (1)

Publication Number Publication Date
JPH04157716A true JPH04157716A (en) 1992-05-29

Family

ID=17657683

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28283490A Pending JPH04157716A (en) 1990-10-19 1990-10-19 Vapor growth apparatus

Country Status (1)

Country Link
JP (1) JPH04157716A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012156510A (en) * 2011-01-21 2012-08-16 Asm Internatl Nv Thermal processing furnace and liner for the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012156510A (en) * 2011-01-21 2012-08-16 Asm Internatl Nv Thermal processing furnace and liner for the same

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