JP2868853B2 - Heat treatment equipment - Google Patents

Heat treatment equipment

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Publication number
JP2868853B2
JP2868853B2 JP17718490A JP17718490A JP2868853B2 JP 2868853 B2 JP2868853 B2 JP 2868853B2 JP 17718490 A JP17718490 A JP 17718490A JP 17718490 A JP17718490 A JP 17718490A JP 2868853 B2 JP2868853 B2 JP 2868853B2
Authority
JP
Japan
Prior art keywords
pressure
exhaust
pipe
exhaust pipe
heat treatment
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 - Lifetime
Application number
JP17718490A
Other languages
Japanese (ja)
Other versions
JPH0464892A (en
Inventor
健一 山賀
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.)
Tokyo Electron Ltd
Original Assignee
Tokyo Electron Ltd
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 Tokyo Electron Ltd filed Critical Tokyo Electron Ltd
Priority to JP17718490A priority Critical patent/JP2868853B2/en
Priority to US07/644,565 priority patent/US5088922A/en
Priority to KR1019910001136A priority patent/KR0147044B1/en
Publication of JPH0464892A publication Critical patent/JPH0464892A/en
Application granted granted Critical
Publication of JP2868853B2 publication Critical patent/JP2868853B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は熱処理装置に関する。The present invention relates to a heat treatment apparatus.

[従来の技術] 従来から、半導体製造工程における気体を伴う一定圧
力下で行われる成膜反応の反応装置では、排気管に設け
られた流量調節弁を調節して装置内を一定圧力に保持す
るようにしたものとして、特開昭62−63421号、特開昭6
3−238281号、特開昭63−304620号公報等がある。
2. Description of the Related Art Conventionally, in a reaction apparatus for a film forming reaction performed under a constant pressure with gas in a semiconductor manufacturing process, a flow control valve provided in an exhaust pipe is adjusted to maintain the inside of the apparatus at a constant pressure. As described above, Japanese Patent Application Laid-Open Nos.
3-238281 and JP-A-63-304620.

しかし、半導体製造装置の熱処理装置等の成膜装置で
は、装置内で行われる反応が一定条件下で行われなけれ
ば形成される膜厚が不均一になってしまい、半導体素子
の歩留りが低下してしまう。そのため、熱処理装置に接
続された排気装置でも排気管内の圧力を微妙にコントロ
ールして熱処理装置内を一定圧に保持しなければならな
かった。
However, in a film forming apparatus such as a heat treatment apparatus of a semiconductor manufacturing apparatus, if a reaction performed in the apparatus is not performed under a certain condition, a formed film thickness becomes non-uniform, and a yield of semiconductor elements is reduced. Would. Therefore, even in the exhaust device connected to the heat treatment device, the pressure in the exhaust pipe must be delicately controlled to maintain the inside of the heat treatment device at a constant pressure.

ところで熱処理装置は、通常複数台設置され、その排
気装置は工場全体の排気系に接続され、強力なファンで
排気されるようになっている。従って、熱処理装置の一
部しか駆動されない場合は排気系が強すぎて排気管の負
圧が大きくなってしまい熱処理装置内の圧力に大きく影
響してしまった。
By the way, a plurality of heat treatment apparatuses are usually installed, and the exhaust device is connected to the exhaust system of the entire factory and exhausted by a powerful fan. Therefore, when only a part of the heat treatment apparatus is driven, the exhaust system is too strong, and the negative pressure in the exhaust pipe increases, which greatly affects the pressure in the heat treatment apparatus.

そのため、排気装置の排気管に支流管を設け、支流管
に重力の方向に対して垂直に配置した弁を設け、この弁
を大気圧と排気管内の圧力差が所定値以上に達すると
(排気管内の圧力が低過ぎる場合)大気圧により弁が押
し上げられ、大気が排気管内に入り、排気管の圧力が上
昇するような重量に予め作成して自動的に開閉できるよ
うな排気圧調整装置が開発された。
Therefore, a branch pipe is provided in the exhaust pipe of the exhaust device, and a valve arranged perpendicular to the direction of gravity is provided in the branch pipe. When the pressure difference between the atmospheric pressure and the pressure in the exhaust pipe reaches a predetermined value or more (exhaust pipe). If the pressure in the pipe is too low) A valve is pushed up by the atmospheric pressure, the atmosphere enters the exhaust pipe, and an exhaust pressure adjusting device that can be automatically opened and closed automatically in advance so that the pressure of the exhaust pipe rises. It has been developed.

[発明が解決すべき課題] しかし、このような排気装置であっても、弁の重さを
排気管内圧と大気圧の圧力差に鋭敏に応答して開閉する
ように例えば−1mmH2Oで作動するように作成するのは難
しく、また工場排気系が大幅に負圧になった場合には弁
が完全に開放状態となり排気管内を所望の一定圧に保持
することができなくなり、熱処理装置内の圧力が変動
し、膜厚も不均一に形成されてしまうという欠点があっ
た。
[Problem to be Solved by the Invention] However, even with such an exhaust device, for example, −1 mmH 2 O is used to open and close the valve weight in response to the difference between the exhaust pipe internal pressure and the atmospheric pressure. It is difficult to make it work, and if the factory exhaust system becomes significantly negative pressure, the valve will be completely open and it will not be possible to maintain the desired constant pressure in the exhaust pipe, and the heat treatment equipment Pressure fluctuates, and the film thickness becomes uneven.

本発明は上記の欠点を解消するためになされたもので
あって、排気装置の排管内圧を一定に保持し、工場排気
系等の排気系に接続されていても過度に減圧になったり
することもなく、工場排気系の変動に対して排気管内の
圧力を一定に保持できる。そのため反応装置内の圧力も
一定に保持され、従って一定条件下で反応が行われるた
め、製品の品質を向上させることができる熱処理装置を
提供することを目的とする。
The present invention has been made in order to solve the above-described drawbacks, and keeps the exhaust pipe internal pressure of an exhaust device constant, and the pressure is excessively reduced even when connected to an exhaust system such as a factory exhaust system. Without pressure, the pressure in the exhaust pipe can be kept constant with respect to fluctuations in the factory exhaust system. Therefore, an object of the present invention is to provide a heat treatment apparatus capable of improving the quality of a product because the pressure in the reaction apparatus is kept constant and the reaction is performed under constant conditions.

[課題を解決するための手段] 上記の目的を達成するため、高温で処理を行う反応装
置と、反応装置から排出されるガスを排気する排気装置
とを備えた熱処理装置において、排気装置は、反応装置
に接続される排気管に設けられ外気圧及び排気管内の圧
力差が所定以上になると、外気圧により開放され大気を
排気管内に流入させる可動弁を備えた支流管と、支流管
の上流に設けられる第1の圧力調整弁及び支流管の下流
に設けられる第2の圧力調整弁とを備え、第1の圧力調
整弁はその上流の排気管の内圧を所定の圧力に調整して
なり、第2の圧力調整弁は第1の圧力調整弁により調整
される圧力と所定差に設定し、支流管内の圧力を可動弁
が正常に作動する圧力に調整してなるものである。
[Means for Solving the Problems] In order to achieve the above object, in a heat treatment apparatus provided with a reactor for performing a process at a high temperature and an exhaust device for exhausting gas discharged from the reactor, the exhaust device comprises: A branch pipe provided with a movable valve that is provided in an exhaust pipe connected to the reaction device and that is opened by the external pressure when the pressure difference between the outside air pressure and the inside of the exhaust pipe becomes a predetermined value or more and allows the air to flow into the exhaust pipe; And a second pressure regulating valve provided downstream of the branch pipe, wherein the first pressure regulating valve regulates the internal pressure of the exhaust pipe upstream thereof to a predetermined pressure. The second pressure regulating valve is set at a predetermined difference from the pressure regulated by the first pressure regulating valve, and regulates the pressure in the branch pipe to a pressure at which the movable valve operates normally.

[作用] 排気管内の圧力と外気圧の差が所定の値以上になった
時(排気管内が過度に減圧されてしまった場合)、その
自重に対抗した外気圧に押され開口して外気を流入させ
排気管内圧を所定の値に上昇させることができる自動開
閉の弁を設けた支流管を排気装置の排気管に設ける。そ
の支流管の上流と下流に圧力調整弁を設け、排気管内の
ガス流量を調整することにより、支流管に設けられた弁
を最良の条件で動作させることができ、反応管と外気圧
の差を所望の一定圧にすることができる。
[Operation] When the difference between the pressure in the exhaust pipe and the outside air pressure exceeds a predetermined value (when the inside of the exhaust pipe is excessively depressurized), the outside air is opened by being pushed by the outside air pressure against its own weight. A tributary pipe provided with an automatic opening / closing valve capable of inflowing and increasing the internal pressure of the exhaust pipe to a predetermined value is provided in the exhaust pipe of the exhaust device. By providing pressure regulating valves upstream and downstream of the branch pipe and adjusting the gas flow rate in the exhaust pipe, the valve provided in the branch pipe can be operated under the best conditions, and the difference between the reaction pipe and the outside air pressure To a desired constant pressure.

[実施例] 以下、本発明の熱処理装置を半導体製造工程の熱処理
装置に適用した一実施例を図面を参照して説明する。
Embodiment An embodiment in which the heat treatment apparatus of the present invention is applied to a heat treatment apparatus in a semiconductor manufacturing process will be described below with reference to the drawings.

第1図に示す反応装置1は、円筒状のプロセスチュー
ブ5を備え、プロセスチューブ5の内部には処理される
半導体ウェハ2を支持する石英ボート3などを載置する
載置台4が備えられる。プロセスチューブ5はその周囲
を例えば円筒状の抵抗加熱コイルヒータ6で囲繞され、
開口部が蓋体7で閉じられ、上記プロセスチューブ5の
内部が500〜1200℃に適宜設定加熱できるようになって
いる。プロセスチューブ5の上部には流量計8を介して
反応ガス供給系9に接続される反応ガス供給口10が設け
られ、プロセスチューブ5の下部には排気装置11に接続
される反応ガス排気口12が備えられ、半導体ウェハ2に
成膜等の処理をした余剰の反応ガスや反応生成ガスの混
合ガスGが排気口12から排気装置11に流入されるように
なっている。排気装置11には熱処理装置1の排気口12に
接続される排気管13と、排気管13に設けられる支流管14
と、支流管14の上流及び下流に設けられる第1及び第2
の圧力調整弁15−1及び15−2等が備えられる。そし
て、この圧力調整弁15−1及び15−2のそれぞれにマノ
メータ等の差圧計16−1及び16−2が設けられる。支流
管14は第2図に示すように一端は排気管13に接続され、
他端は軸が鉛直になるよう屈曲させて成る。そして鉛直
部17に大径部18を設け、大径部18に弾性部材から成るO
リング19を取着させ、Oリング19上に可動弁20が配置さ
れる。可動弁20は例えば外気圧と排気管13内の差圧が−
10mmH2Oを所望とすれば、1気圧=10000mmH2O=1Kg/cm2
の関係から1g/cm2の重さにすればよい。可動弁20の重さ
の調整は材質や厚さにより行う。
The reaction apparatus 1 shown in FIG. 1 includes a cylindrical process tube 5, and a mounting table 4 on which a quartz boat 3 supporting a semiconductor wafer 2 to be processed is mounted. The process tube 5 is surrounded by, for example, a cylindrical resistance heating coil heater 6,
The opening is closed by the lid 7 so that the inside of the process tube 5 can be appropriately heated to 500 to 1200 ° C. A reaction gas supply port 10 connected to a reaction gas supply system 9 via a flow meter 8 is provided at an upper portion of the process tube 5, and a reaction gas exhaust port 12 connected to an exhaust device 11 is provided at a lower portion of the process tube 5. The surplus reaction gas or the mixed gas G of the reaction product gas, which has been subjected to a process such as film formation on the semiconductor wafer 2, flows into the exhaust device 11 from the exhaust port 12. The exhaust device 11 includes an exhaust pipe 13 connected to the exhaust port 12 of the heat treatment apparatus 1 and a branch pipe 14 provided in the exhaust pipe 13.
And first and second provided upstream and downstream of the branch pipe 14.
Pressure regulating valves 15-1 and 15-2 are provided. Each of the pressure regulating valves 15-1 and 15-2 is provided with a differential pressure gauge 16-1 or 16-2 such as a manometer. The branch pipe 14 has one end connected to the exhaust pipe 13 as shown in FIG.
The other end is bent so that the axis is vertical. A large-diameter portion 18 is provided in the vertical portion 17, and the large-diameter portion 18
The ring 19 is attached, and the movable valve 20 is arranged on the O-ring 19. The movable valve 20 has, for example, a pressure difference between the outside air pressure and the exhaust pipe 13 −
If 10 mmH 2 O is desired, 1 atmosphere = 10000 mmH 2 O = 1 kg / cm 2
Therefore, the weight may be 1 g / cm2. The weight of the movable valve 20 is adjusted depending on the material and the thickness.

このような排気装置11を備えた熱処理装置1は通常工
場内に多数設置され、これらの排気装置11の排気管13は
それぞれ例えば工場排気系等の排気能力の大きな排気系
ファン21に共通排気管22を介して接続される。
A large number of heat treatment apparatuses 1 having such an exhaust device 11 are usually installed in a factory, and the exhaust pipes 13 of these exhaust devices 11 are respectively connected to an exhaust system fan 21 having a large exhaust capacity such as a factory exhaust system. Connected via 22.

このような構成の熱処理装置の排気装置の動作を説明
する。
The operation of the exhaust device of the heat treatment apparatus having such a configuration will be described.

複数の熱処理装置1のうち、1台のみが稼動し、他は
停止されている場合を述べる。流量計8により反応ガス
供給系9から供給される反応ガスの所定量を測定し、所
定量の反応ガスをプロセスチューブ5の反応ガス供給口
10から供給する。コイルヒータ6により例えば1000℃に
加熱されたプロセスチューブ5内で半導体ウェハ2が処
理される。処理後、余剰の反応ガス及び生成ガスの混合
ガスGは排気口12から排気管13に流入される。この時、
他の熱処理装置1は稼動されず、従って他の排気装置に
は混合ガスGが流れないため排気ファン21の排気能力に
対して混合ガスGの流量の割合が少なくなる。支流管14
の可動弁20のみの働きであると、排気管内圧の所望の差
圧が例えば−1〜0mmH2O以下であっても、排気管13の負
圧が非常に大きくなるまで可動しない。例えば−10mmH2
O以下になると支流管14に設けられた可動弁20が外気圧
に押されてOリング19から浮上する。そして外気が排気
管13内に流入され、排気管13は過剰な負圧状態でなく−
10mmH2Oに保たれる。この時、排気管13の支流管14の上
流に設けられた圧力調整弁15−1を調整し、混合ガスG
の流量を調整し差圧計16−1の検出値が所望の−1〜0m
mH2Oになるようにする。また、支流管14の下流の圧力調
整弁15−2は、支流管14の開口部を塞いだ状態で排気管
13内が所望の差圧例えば−15〜−20mmH2Oを示すよう
に、差圧計16−2の検出値を検出しながら調整する。以
上ように圧力調整弁15−1、15−2を調整することによ
り支流管14で行なう圧力調整を最適な圧力条件で行なう
ことができる。
A case will be described in which only one of the plurality of heat treatment apparatuses 1 is operating and the others are stopped. A predetermined amount of the reaction gas supplied from the reaction gas supply system 9 is measured by the flow meter 8 and a predetermined amount of the reaction gas is supplied to the reaction gas supply port of the process tube 5.
Supplied from 10. The semiconductor wafer 2 is processed in the process tube 5 heated to, for example, 1000 ° C. by the coil heater 6. After the treatment, the excess mixed gas G of the reaction gas and the generated gas flows from the exhaust port 12 into the exhaust pipe 13. At this time,
The other heat treatment apparatus 1 is not operated, so that the mixed gas G does not flow to the other exhaust device, so that the ratio of the flow rate of the mixed gas G to the exhaust capacity of the exhaust fan 21 decreases. Branch pipe 14
If it is the action of only the movable valve 20 of, even desired differential pressure of the exhaust pipe pressure, for example -1~0mmH 2 O or less, not moving to the negative pressure in the exhaust pipe 13 becomes very large. For example -10mmH 2
When the pressure becomes O or less, the movable valve 20 provided in the branch pipe 14 is pushed by the outside air pressure and floats from the O-ring 19. Then, the outside air flows into the exhaust pipe 13, and the exhaust pipe 13 is
It is kept at 10mmH 2 O. At this time, the pressure regulating valve 15-1 provided upstream of the branch pipe 14 of the exhaust pipe 13 is adjusted to adjust the mixed gas G
And the detected value of the differential pressure gauge 16-1 is the desired -1 to 0 m
to be mH 2 O. The pressure regulating valve 15-2 downstream of the branch pipe 14 is connected to the exhaust pipe with the opening of the branch pipe 14 closed.
13 is to show the desired differential pressure for example -15~-20mmH 2 O, adjusted while detecting the detection value of the differential pressure gauge 16-2. By adjusting the pressure adjusting valves 15-1 and 15-2 as described above, the pressure adjustment performed in the branch pipe 14 can be performed under optimal pressure conditions.

そのため、支流管14の可動弁20は常に最適な圧力条件
である−10mmH2O前後で動作し、圧力調整弁15−1を調
整することで圧力調整弁15−1の上流部を所望の圧力に
保持することができる。工場排気系と稼働される装置と
の関係で圧力調整弁15−2を適宜調整しておくことによ
り、工場排気系のによる吸引力の変動により生じる圧力
変動に拘らず熱処理も一定条件下で行うことができる。
Therefore, the movable valve 20 of the branch pipe 14 always operates at the optimum pressure condition of about −10 mmH 2 O, and by adjusting the pressure regulating valve 15-1, the upstream part of the pressure regulating valve 15-1 is brought to a desired pressure. Can be held. By appropriately adjusting the pressure control valve 15-2 in relation to the factory exhaust system and the device to be operated, heat treatment is also performed under a constant condition regardless of the pressure variation caused by the variation of the suction force by the factory exhaust system. be able to.

また他の実施例として、第1図に示すように差圧計16
0−1及び160−2の出力により圧力調整弁150−1及び1
50−2を自動的に駆動しフィードバック制御を行うよう
にしてもよい。
As another embodiment, as shown in FIG.
The pressure control valves 150-1 and 150-1 are output by the outputs of 0-1 and 160-2.
50-2 may be automatically driven to perform feedback control.

本発明は上記の実施例に限定されるものでなく、工場
排気系に接続されず、単一の装置にも適用できる。ま
た、熱処理装置にも限定されず、CVD装置や処理液例え
ばレジストを塗布するスピンコータ装置等反応圧を一定
に保って処理を行う装置に好適に用いることができる。
The present invention is not limited to the above embodiment, and is applicable to a single device without being connected to a factory exhaust system. Further, the present invention is not limited to a heat treatment apparatus, and can be suitably used for an apparatus for performing processing while maintaining a constant reaction pressure, such as a CVD apparatus or a spin coater apparatus for applying a processing liquid such as a resist.

[発明の効果] 以上の説明からも明らかなように、本発明の熱処理装
置は、外気圧と排気管内の差圧が大きくなった時に作動
する可動弁を備えた支流管の上流と下流のそれぞれに圧
力調整弁を設けたため、支流管で行う圧力調整を最適な
圧力条件で行うことができ、高精度に均一な排気管内圧
を保持でき、従って反応装置内の圧力も所望の一定圧に
維持できる。そのため、半導体ウェハの均一処理がで
き、高品位な製品の製造を行うことができる。
[Effects of the Invention] As is clear from the above description, the heat treatment apparatus of the present invention can be used for the upstream and downstream of the branch pipe having a movable valve that operates when the differential pressure between the outside air pressure and the exhaust pipe increases. The pressure adjustment valve provided at the outlet allows the pressure adjustment performed in the branch pipe to be performed under the optimal pressure condition, thereby maintaining the pressure inside the exhaust pipe with high accuracy and uniformity, and thus maintaining the pressure inside the reactor at a desired constant pressure. it can. Therefore, uniform processing of the semiconductor wafer can be performed, and high-quality products can be manufactured.

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

第1図は本発明の一実施例を示す構成図、第2図は第1
図に示す一実施例の要部を示す図である。 1……反応装置 11……排気装置 13……排気管 14……支流管 15−1、15−2、150−1、150−2……圧力調整弁
FIG. 1 is a block diagram showing one embodiment of the present invention, and FIG.
It is a figure showing an important section of one example shown in a figure. DESCRIPTION OF SYMBOLS 1 ... Reactor 11 ... Exhaust device 13 ... Exhaust pipe 14 ... Branch pipe 15-1, 15-2, 150-1, 150-2 ... Pressure regulating valve

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】高温で処理を行う反応装置と、前記反応装
置から排出されるガスを排気する排気装置とを備えた熱
処理装置において、前記排気装置は、前記反応装置に接
続される排気管に設けられ外気圧及び前記排気管内の圧
力差が所定以上になると、外気圧により開放され大気を
前記排気管内に流入させる可動弁を備えた支流管と、前
記支流管の上流に設けられる第1の圧力調整弁及び前記
支流管の下流に設けられる第2の圧力調整弁とを備え、
前記第1の圧力調整弁はその上流の排気管の内圧を所定
の圧力に調整してなり、前記第2の圧力調整弁は前記第
1の圧力調整弁により調整される圧力と所定差に設定
し、前記支流管内の圧力を前記可動弁が正常に作動する
圧力に調整してなることを特徴とする熱処理装置。
1. A heat treatment apparatus comprising: a reactor for performing a process at a high temperature; and an exhaust device for exhausting gas discharged from the reactor, wherein the exhaust device is connected to an exhaust pipe connected to the reactor. A tributary pipe provided with a movable valve which is opened by the external pressure and allows the air to flow into the exhaust pipe, and a first tributary pipe provided upstream of the tributary pipe when the pressure difference between the external pressure and the exhaust pipe becomes equal to or more than a predetermined value. A pressure regulating valve and a second pressure regulating valve provided downstream of the branch pipe,
The first pressure regulating valve regulates the internal pressure of the exhaust pipe upstream thereof to a predetermined pressure, and the second pressure regulating valve is set to a prescribed difference from the pressure regulated by the first pressure regulating valve. The pressure in the tributary pipe is adjusted to a pressure at which the movable valve operates normally.
JP17718490A 1990-01-23 1990-07-04 Heat treatment equipment Expired - Lifetime JP2868853B2 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP17718490A JP2868853B2 (en) 1990-07-04 1990-07-04 Heat treatment equipment
US07/644,565 US5088922A (en) 1990-01-23 1991-01-23 Heat-treatment apparatus having exhaust system
KR1019910001136A KR0147044B1 (en) 1990-01-23 1991-01-23 Heat treatment apparatus having exhaust system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17718490A JP2868853B2 (en) 1990-07-04 1990-07-04 Heat treatment equipment

Publications (2)

Publication Number Publication Date
JPH0464892A JPH0464892A (en) 1992-02-28
JP2868853B2 true JP2868853B2 (en) 1999-03-10

Family

ID=16026650

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17718490A Expired - Lifetime JP2868853B2 (en) 1990-01-23 1990-07-04 Heat treatment equipment

Country Status (1)

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JP (1) JP2868853B2 (en)

Also Published As

Publication number Publication date
JPH0464892A (en) 1992-02-28

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