JPH03183693A - Method and apparatus for cleaning vapor growth device - Google Patents

Method and apparatus for cleaning vapor growth device

Info

Publication number
JPH03183693A
JPH03183693A JP31767589A JP31767589A JPH03183693A JP H03183693 A JPH03183693 A JP H03183693A JP 31767589 A JP31767589 A JP 31767589A JP 31767589 A JP31767589 A JP 31767589A JP H03183693 A JPH03183693 A JP H03183693A
Authority
JP
Japan
Prior art keywords
cleaning gas
reactor
reactive cleaning
exhaust pipe
gas
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
JP31767589A
Other languages
Japanese (ja)
Inventor
Yukio Komura
幸夫 香村
Michio Takahashi
高橋 道生
Sadanori Ishida
禎則 石田
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.)
Furukawa Electric Co Ltd
Original Assignee
Furukawa Electric Co 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 Furukawa Electric Co Ltd filed Critical Furukawa Electric Co Ltd
Priority to JP31767589A priority Critical patent/JPH03183693A/en
Publication of JPH03183693A publication Critical patent/JPH03183693A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To clean a vapor growth device with low-cost facilities by feeding a reactive cleaning gas not activated with ions into the reactor of the device and an exhaust pipe connected to the reactor. CONSTITUTION:A reactive cleaning gas 9 not activated with ions is fed into the reactor 1 of a vapor growth device 8 and an exhaust pipe 4 connected to the reactor 1 to remove a reaction product sticking to the insides of the reactor 1 and the pipe 4. HF3, ClF3 or Cl2, etc., may be used as the reactive cleaning gas. Cleaning is carried out without requiring an ion source and the reactive cleaning gas maintains its reactivity and can clean even the inside of the exhaust pipe without hindrance.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、気相成長装置のクリーニング方法及び装置に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for cleaning a vapor phase growth apparatus.

[従来の技術] 例えば、GaAsウェハー上にGaAs薄膜やAl2G
aAs薄膜を有機金属化学堆積法(以下、MOCVD法
という)により成膜したエピタキシャルウェハーは、電
界効果トランジスタ(FET)や高電子移動度トランジ
スタ(HEMT)用として近年注目されている。また、
InPn上ウェハー上nP、InGaAs、InGaA
sP等の薄膜をMOCVD法により成膜したエピタキシ
ャルウェハーは、レーザダイオード等用として使用され
つつある。MOCVD法は、リアクタ内で8[)[1℃
位に加熱された■族の有機金属TMIn即ち(In (
CH3)3)、TMG即ち(Ga  (CH3)3)と
V族のPH3,ASH3をガス状にして流し、InPウ
ェハー上に成膜することにより行う。このとき、加熱さ
れたリアクタ及びサセプタ上にも反応生成物が付着する
ので、リアクタ内を清浄にするため定期的に該リアクタ
やサセプタ等は分解して洗浄を行っていた。また、リア
クタの後に接続されている排気管の内面にも反応生成物
が付着する。減圧MOCVD法の場合には、減圧ポンプ
の中にも反応生成物が付着する。特に、P(燐)を使う
プロセスでは、Pと空気中の酸素が反応し、リアクタ等
の分解清掃時にPに着火して非常に危険な状態になる。
[Prior art] For example, a GaAs thin film or an Al2G film is deposited on a GaAs wafer.
Epitaxial wafers in which aAs thin films are formed by a metal organic chemical deposition method (hereinafter referred to as MOCVD method) have recently attracted attention for use in field effect transistors (FETs) and high electron mobility transistors (HEMTs). Also,
InPn on wafer nP, InGaAs, InGaA
Epitaxial wafers on which thin films such as sP are formed by MOCVD are being used for laser diodes and the like. In the MOCVD method, the temperature in the reactor is 8[)[1℃
Group II organometallic TMIn, i.e. (In (
CH3)3), TMG, ie, (Ga (CH3)3), PH3 and ASH3 of group V are made into gases and flowed to form a film on an InP wafer. At this time, reaction products also adhere to the heated reactor and susceptor, so the reactor, susceptor, etc. are periodically disassembled and cleaned in order to clean the inside of the reactor. In addition, reaction products also adhere to the inner surface of the exhaust pipe connected after the reactor. In the case of the reduced pressure MOCVD method, reaction products also adhere to the inside of the reduced pressure pump. In particular, in processes that use P (phosphorus), the P reacts with oxygen in the air, and when a reactor or the like is disassembled and cleaned, the P ignites, creating a very dangerous situation.

これを避けるため、イオン源で活性化されたイオン活性
化反応性クリーニングガスをリアクタ及び排気管に流し
てクリーニングを行う方法が提案されている。
In order to avoid this, a method has been proposed in which cleaning is performed by flowing an ion-activated reactive cleaning gas activated by an ion source into the reactor and exhaust pipe.

[発明が解決しようとする課題] しかしながら、このようにイオン源で活性化されたイオ
ン活性化反応性クリーニングガスでは、イオン源を必要
とし、コスト高になる問題点がある。また、イオン源で
活性化されたイオン活性化反応性クリーニングガスでは
、イオンの寿命が短いため排気管のクリーニングが行い
にくい問題点があった。
[Problems to be Solved by the Invention] However, such an ion-activated reactive cleaning gas activated by an ion source has the problem of requiring an ion source and increasing costs. Furthermore, the ion-activated reactive cleaning gas activated by the ion source has a problem in that it is difficult to clean the exhaust pipe because the ions have a short lifespan.

本発明の目的は、安価な設備でクリーニングを行うこと
ができる気相成長装置のクリーニング方法及び装置を提
供することにある。
An object of the present invention is to provide a method and apparatus for cleaning a vapor phase growth apparatus, which allows cleaning to be performed using inexpensive equipment.

[課題を解決するための手段] 上記の目的を達成するための本発明の詳細な説明する。[Means to solve the problem] The present invention will now be described in detail to achieve the above objects.

請求項(1)に記載の気相成長装置のクリーニング方法
は、気相成長装置のリアクタ内及びこれに接続されてい
る排気管内に、イオン活性化されていない反応性クリー
ニングガスを流して該リアクタ及び該排気管の内面に付
着されている反応生成物を除去することを特徴とする。
The method for cleaning a vapor-phase growth apparatus according to claim (1) includes flowing a reactive cleaning gas that is not ion-activated into the reactor of the vapor-phase growth apparatus and the exhaust pipe connected to the reactor. and removing reaction products attached to the inner surface of the exhaust pipe.

イオン活性化されていない反応性クリーニングガスとし
ては、例えばNF3.C,QF3.CJ22等を用いる
Examples of reactive cleaning gases that are not ion activated include NF3. C, QF3. CJ22 or the like is used.

請求項(2)に記載の発明は、リアクタと、該リアクタ
に接続されている排気管と、該排気管に接続されている
原料ガス用廃ガス処理部とを備えた気相成長装置のクリ
ーニング装置において、前記リアクタ内に開閉バルブを
介してイオン活性化されていない反応性クリーニングガ
スを供給する反応性クリーニングガス供給配管と、前記
原料ガス用廃ガス処理部とは別に前記排気管に反応性ク
リーニングガス排気管を介して接続されていて前記反応
性クリーニングガスの処理を行う反応性クリーニングガ
ス用廃ガス処理部と、前記原料ガス用廃ガス処理部又は
前記反応性クリーニングガス用廃ガス処理部のいずれか
を選択的に使用するために前記排気管と前記反応性クリ
ーニングガス排気管とに接続されている切替えバルブと
を有することを特徴とする。
The invention according to claim (2) provides a method for cleaning a vapor phase growth apparatus that includes a reactor, an exhaust pipe connected to the reactor, and a raw material gas waste gas treatment section connected to the exhaust pipe. In the apparatus, a reactive cleaning gas supply pipe that supplies a non-ion activated reactive cleaning gas into the reactor via an on-off valve, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion activated into the reactor, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion-activated into the reactor, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion-activated into the reactor, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion-activated into the reactor, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion-activated into the reactor, and a reactive cleaning gas supply pipe that supplies a reactive cleaning gas that is not ion-activated into the reactor, and a reactive cleaning gas waste gas treatment section that is connected via a cleaning gas exhaust pipe and processes the reactive cleaning gas; and the raw material gas waste gas treatment section or the reactive cleaning gas waste gas treatment section. The invention is characterized in that it has a switching valve connected to the exhaust pipe and the reactive cleaning gas exhaust pipe in order to selectively use one of the reactive cleaning gas exhaust pipes.

[作用] このようなイオン活性化されていない反応性クリーニン
グガスは、イオン源を必要としないでクリーニングが行
える。また、この反応性クリーニングガスはイオン化さ
れてなく、反応性が持続するので、排気管内のクリーニ
ングも支障なく行える。
[Function] Such a reactive cleaning gas that is not ion activated can perform cleaning without requiring an ion source. Further, since this reactive cleaning gas is not ionized and remains reactive, the inside of the exhaust pipe can be cleaned without any problem.

特に、請求項(2)では、原料ガス用廃ガス処理部とは
別に反応性クリーニングガス用廃ガス処理部を設けてい
るので、原料ガス用廃ガス処理部で反応性クリーニング
ガスの処理を行う場合に生ずるような処理中の反応の進
み過ぎとそれに伴う過熱を避けて反応性クリーニングガ
スの無害化処理を行うことができる。
In particular, in claim (2), since the reactive cleaning gas waste gas treatment section is provided separately from the raw material gas waste gas treatment section, the reactive cleaning gas is processed in the raw material gas waste gas treatment section. It is possible to detoxify the reactive cleaning gas while avoiding excessive reaction during processing and the resulting overheating that would otherwise occur.

[実施例] 以下、本発明の実施例を図面を参照して詳細に説明する
。図において、1はサセプタ(図示せず)を内蔵するリ
アクタ、2は該リアクタ1内に原料ガスを供給する原料
ガス供給配管、3は該原料ガス供給配管2に設けられて
いる原料ガス用開閉バルブ、4はリアクタ1に接続され
ている排気管、5は排気管4に設けられている排気用開
閉バルブ、6は排気管4の末端側に接続されている油回
転ポンプ等よりなる原料ガス用吸引機、7は原料ガス用
吸引機6の後に接続されていて原料ガスを無害化処理す
る原料ガス用廃ガス処理部である。これら1〜7にて気
相成長装置8が構成されている。
[Example] Hereinafter, an example of the present invention will be described in detail with reference to the drawings. In the figure, 1 is a reactor with a built-in susceptor (not shown), 2 is a raw material gas supply pipe that supplies raw material gas into the reactor 1, and 3 is a source gas opening and closing provided in the raw material gas supply pipe 2. 4 is an exhaust pipe connected to the reactor 1; 5 is an exhaust opening/closing valve provided in the exhaust pipe 4; 6 is an oil rotary pump connected to the end of the exhaust pipe 4. The suction device 7 is a waste gas treatment section for raw material gas that is connected after the suction device 6 for raw material gas and detoxifies the raw material gas. These 1 to 7 constitute a vapor phase growth apparatus 8.

また、9はリアクタ1又は排気管4に反応性クリーニン
グガスを供給する反応性クリーニングガス供給配管、1
0は反応性クリーニングガス供給配管9から分岐されて
リアクタ1内に反応性クリーングガスを供給する分岐反
応性クリーニングガス供給配管、11は分岐反応性クリ
ーニングガス供給配管10に設けられた反応性クリーニ
ングガス用開閉バルブ、12は反応性クリーニングガス
供給配管9から分岐されて配管4内に反応性クリーニン
グガスを供給する分岐反応性クリーニングガス供給配管
、13は分岐反応性クリーニングガス供給配管12に設
けられた反応性クリーニングガス用開閉バルブである。
Further, 9 is a reactive cleaning gas supply pipe for supplying reactive cleaning gas to the reactor 1 or the exhaust pipe 4;
0 is a branched reactive cleaning gas supply pipe that is branched from the reactive cleaning gas supply pipe 9 and supplies reactive cleaning gas into the reactor 1, and 11 is a reactive cleaning gas provided in the branched reactive cleaning gas supply pipe 10. 12 is a branched reactive cleaning gas supply pipe that is branched from the reactive cleaning gas supply pipe 9 and supplies reactive cleaning gas into the pipe 4; 13 is provided in the branched reactive cleaning gas supply pipe 12; This is an on-off valve for reactive cleaning gas.

14は原料ガス用吸引機6の人口側で排気管4に分岐接
続された反応性クリーニングガス排気管、15は反応性
クリーニングガス排気管14の途中にバイパス反応性ク
リーニングガス排気管16を介してバイパス接続されて
いる油回転ポンプ等よりなる反応性クリーニングガス用
吸引機、17.18はバイパス反応性クリーニングガス
排気管16の入口と出口に設けられた反応性クリーニン
グガス用開閉バルブ、19はバイパス反応性クリーニン
グガス排気管16に並列となっている反応性クリーニン
グガス排気管14の部分に設けられた反応性クリーニン
グガス用開閉バルブ、20は反応性クリーニングガス排
気管14の末端側に接続されていて反応性クリーニング
ガスを無害化処理する反応性クリーニングガス用廃ガス
処理部である。21.22は原料ガス用廃ガス処理部7
を使うか反応性クリーニングガス用廃ガス処理部20を
使うかの切替えを行うために排気管4と反応性クリーニ
ングガス排気管↑4とに接続された切替えバルブである
。これら9〜22にて気相成長装置8のクリーニング装
置23が構成されている。
Reference numeral 14 indicates a reactive cleaning gas exhaust pipe connected to the exhaust pipe 4 on the intake side of the raw material gas suction device 6, and reference numeral 15 indicates a reactive cleaning gas exhaust pipe 16 which is connected in the middle of the reactive cleaning gas exhaust pipe 14 through a bypass reactive cleaning gas exhaust pipe 16. A suction device for reactive cleaning gas consisting of an oil rotary pump or the like connected to a bypass, 17.18 an on-off valve for reactive cleaning gas provided at the inlet and outlet of the bypass reactive cleaning gas exhaust pipe 16, 19 a bypass A reactive cleaning gas opening/closing valve 20 is provided at a portion of the reactive cleaning gas exhaust pipe 14 that is parallel to the reactive cleaning gas exhaust pipe 16, and is connected to the end side of the reactive cleaning gas exhaust pipe 14. This is a waste gas processing unit for reactive cleaning gas that detoxifies the reactive cleaning gas. 21.22 is the raw material gas waste gas processing section 7
This is a switching valve connected to the exhaust pipe 4 and the reactive cleaning gas exhaust pipe ↑4 in order to switch between using the exhaust gas treatment section 20 for reactive cleaning gas and the exhaust gas treatment section 20 for reactive cleaning gas. These 9 to 22 constitute a cleaning device 23 of the vapor phase growth apparatus 8.

次に、このようなりリーニング装置23による気相成長
装置8のクリーニング方法について説明する。
Next, a method of cleaning the vapor phase growth apparatus 8 using the cleaning apparatus 23 will be described.

減圧MOCVD法の場合、エピタキシャルウェハーの製
造中は、バルブ3. 5. 21を開、他のバルブは全
て閉として、原料ガス用吸引機6を作動し、リアクタ1
から排出される原料ガスの廃ガスを原料ガス用廃ガス処
理部7に導いて無害化処理する。即ち、この原料ガス用
廃ガス処理部7では、例えばPH3、AsH3、TMG
、TMI n等の無害化処理を行う。
In the case of the low pressure MOCVD method, during the production of epitaxial wafers, valve 3. 5. 21 is opened, all other valves are closed, the raw material gas suction machine 6 is operated, and the reactor 1 is opened.
The waste gas of the raw material gas discharged from the raw material gas is guided to the raw material gas waste gas processing section 7 and is rendered harmless. That is, in this raw material gas waste gas treatment section 7, for example, PH3, AsH3, TMG
, TMI n, etc.

エピタキシャルウェハーの製造後は、原料ガス供給配管
2からリアクタ1及び排気管4に窒素又はArからなる
パージガスを流して原料ガスのパージを行う。
After manufacturing the epitaxial wafer, a purge gas made of nitrogen or Ar is flowed from the source gas supply pipe 2 to the reactor 1 and the exhaust pipe 4 to purge the source gas.

次に、バルブ3を閉とし、原料ガス用吸引機6の作動に
よりリアクタ1及び排気管4内を真空引きする。
Next, the valve 3 is closed, and the inside of the reactor 1 and the exhaust pipe 4 are evacuated by operating the raw material gas suction device 6.

次いで、バルブ11.22.19を開、バルブ21を閉
として反応性クリーニングガス供給配管9及び分岐反応
性クリーニングガス供給配管10を経てリアクタ1及び
排気管4内にイオン活性化されていない反応性クリーニ
ングガスを数時間流し、リアクタ1内及び排気管4内の
クリーニングを行う。イオン活性化されていない反応性
クリーニングガスとしては、例えばNF3.CJ2F3
゜C12等を用いる。このような反応性クリーニングガ
スを用いると、リアクタ1内及び排気管4内の付着物は
例えばC℃系化合物のガスやF系化合物のガス等となっ
て除去できる。使用済の反応性クリーニングガスは反応
性クリーニングガス用廃ガス処理部20で逐次無害化処
理してから大気中に放出する。即ち、反応性クリーニン
グガス用廃ガス処理部20では、例えばC℃系化合物や
F系化合物等の無害化処理を行う。
Then, by opening the valves 11, 22, and 19 and closing the valve 21, the non-activated ions are introduced into the reactor 1 and the exhaust pipe 4 through the reactive cleaning gas supply pipe 9 and the branched reactive cleaning gas supply pipe 10. The inside of the reactor 1 and the exhaust pipe 4 are cleaned by flowing the cleaning gas for several hours. Examples of reactive cleaning gases that are not ion activated include NF3. CJ2F3
Use ゜C12 etc. When such a reactive cleaning gas is used, deposits inside the reactor 1 and the exhaust pipe 4 can be removed by converting them into, for example, C° C.-based compound gas or F-based compound gas. The used reactive cleaning gas is sequentially rendered harmless in the reactive cleaning gas waste gas treatment section 20 and then released into the atmosphere. That is, in the reactive cleaning gas waste gas processing section 20, for example, C° C.-based compounds, F-based compounds, and the like are rendered harmless.

次に、バルブ11を閉、バルブ3を開として、リアクタ
1.排気管49反応性クリーニングガス排気管14に原
料ガス供給配管2からパージガスを流し、反応性クリー
ニングガスのパージを行う。
Next, valve 11 is closed, valve 3 is opened, and reactor 1. Exhaust pipe 49 Reactive cleaning gas Purge gas is flowed from raw material gas supply pipe 2 to reactive cleaning gas exhaust pipe 14 to purge the reactive cleaning gas.

しかる後、バルブ19を閉、バルブ17.18を開とし
、反応性クリーニングガス用吸引機15を使ってリアク
タ1.排気管4内を減圧する。この工程によって、リア
クタ1及び排気管4内の反応性クリーニングガスの濃度
が下がる。
Thereafter, valve 19 is closed, valve 17.18 is opened, and reactive cleaning gas suction device 15 is used to pump reactor 1. The pressure inside the exhaust pipe 4 is reduced. This step reduces the concentration of the reactive cleaning gas in the reactor 1 and the exhaust pipe 4.

次に、バルブ11を閉、バルブ3を開、バルブ22を閉
、反応性クリーニングガス用吸引機15を停止、バルブ
21を開として、リアクタ1及び排気管4内にパージガ
スを流してこれらの中を元の状態に戻す。
Next, close the valve 11, open the valve 3, close the valve 22, stop the reactive cleaning gas suction device 15, and open the valve 21 to flow the purge gas into the reactor 1 and the exhaust pipe 4. return to its original state.

なお、原料ガス用供給機69反応性クリーニングガス用
吸引機15としては、油回転ポンプ以外に、メカニカル
ブースタポンプ、乾式排気ポンプ。
In addition to the oil rotary pump, the raw material gas supply device 69 and the reactive cleaning gas suction device 15 include a mechanical booster pump and a dry exhaust pump.

ターボポンプ等を使用することができる。A turbo pump etc. can be used.

また、反応性クリーニングガスとしてClF3を使う場
合、リアクタ1及び排気管4内の温度がクリーニング反
応で急激に上ることもあるので、リアクタ1及び排気管
4の近くに温度センサを設けて常時モニタすることが好
ましい。
Furthermore, when using ClF3 as a reactive cleaning gas, the temperature inside the reactor 1 and exhaust pipe 4 may rise rapidly due to the cleaning reaction, so a temperature sensor should be installed near the reactor 1 and exhaust pipe 4 to constantly monitor it. It is preferable.

更に、リアクタ1やサセプタはある程度クリーニングし
た後に、分解洗浄することもできる。この場合、これら
は予めクリーニングされているので、Pに着火するよう
なことは起こらないので安全である。また、排気管4内
もクリーニングすることにより閉塞したり不純物がリア
クタ1内に逆流してエピタキシャルウェハーを汚染する
ことも防ぐことができる。
Furthermore, the reactor 1 and the susceptor can be cleaned to some extent and then disassembled for cleaning. In this case, since these have been cleaned in advance, ignition of P will not occur, so it is safe. Furthermore, by cleaning the inside of the exhaust pipe 4, it is possible to prevent clogging and impurities from flowing back into the reactor 1 and contaminating the epitaxial wafer.

かつまた、排気管4内に水分があると、HC℃やHFが
できる可能性があるので、排気管4内に露点計を設けて
常にモニタすることが好ましい。
Furthermore, if there is moisture in the exhaust pipe 4, there is a possibility that HC°C or HF may be formed, so it is preferable to provide a dew point meter in the exhaust pipe 4 and constantly monitor it.

[発明の効果] 以上説明したように本発明に係る気相成長装置のクリー
ニング方法及び装置によれば、下記のような効果を得る
ことができる。
[Effects of the Invention] As explained above, according to the method and apparatus for cleaning a vapor phase growth apparatus according to the present invention, the following effects can be obtained.

請求項(1)(2)では、イオン活性化されてない反応
性クリーニングガスを用いてクリーニングを行うので、
イオン源を必要としないでクリーニングが行える利点が
ある。また、この反応性クリーニングガスはイオン化さ
れてなく、反応性が持続するので、排気管内のクリーニ
ングも支障なく行える利点がある。
In claims (1) and (2), since cleaning is performed using a reactive cleaning gas that is not ion activated,
There is an advantage that cleaning can be performed without requiring an ion source. Further, since this reactive cleaning gas is not ionized and remains reactive, it has the advantage that the inside of the exhaust pipe can be cleaned without any trouble.

特に、請求項(2)では、原料ガス用廃ガス処理部とは
別に反応性クリーニングガス用廃ガス処理部を設けてい
るので、原料ガス用廃ガス処理部で反応性クリーニング
ガスの処理を行う場合に生ずるような処理中の反応の進
み過ぎとそれに伴う過熱を避けて反応性クリーニングガ
スの無害化処理を行うことができる利点がある。
In particular, in claim (2), since the reactive cleaning gas waste gas treatment section is provided separately from the raw material gas waste gas treatment section, the reactive cleaning gas is processed in the raw material gas waste gas treatment section. There is an advantage that the reactive cleaning gas can be detoxified while avoiding the excessive progress of the reaction during the treatment and the accompanying overheating that would otherwise occur.

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

図面は本発明に係るクリーニング装置を取付けた気相成
長装置の一実施例の系統図である。 1・・・リアクタ、2・・・原料ガス供給配管、3・・
・開閉バルブ、4・・・排気管、5・・・開閉バルブ、
6・・・原料ガス用吸引機、7・・・原料ガス用廃ガス
処理部、8・・・気相成長装置、9・・・反応性クリー
ニングガス供給配管、10.12・・・分岐反応性クリ
ーニングガス供給配管、11.13・・・開閉バルブ、
14・・・反応性クリーニングガス排気管、■5・・・
反応性クリーニングガス用吸引機、16・・・バイパス
反応性クリーニングガス排気管、17.18・・・開閉
バルブ、19・・・開閉バルブ、20・・・反応性クリ
ーニングガス用廃ガス処理部、21.22・・・切替え
バルブ、 23・・・クリーニング装置。
The drawing is a system diagram of an embodiment of a vapor phase growth apparatus equipped with a cleaning device according to the present invention. 1...reactor, 2...raw material gas supply piping, 3...
・Opening/closing valve, 4...Exhaust pipe, 5...Opening/closing valve,
6... Suction device for raw material gas, 7... Waste gas treatment section for raw material gas, 8... Vapor phase growth device, 9... Reactive cleaning gas supply piping, 10.12... Branch reaction cleaning gas supply piping, 11.13... opening/closing valve,
14...Reactive cleaning gas exhaust pipe, ■5...
Suction device for reactive cleaning gas, 16... bypass reactive cleaning gas exhaust pipe, 17.18... opening/closing valve, 19... opening/closing valve, 20... waste gas treatment section for reactive cleaning gas, 21.22...Switching valve, 23...Cleaning device.

Claims (2)

【特許請求の範囲】[Claims] (1)気相成長装置のリアクタ内及びこれに接続されて
いる排気管内に、イオン活性化されていない反応性クリ
ーニングガスを流して該リアクタ及び該排気管の内面に
付着されている反応生成物を除去することを特徴とする
気相成長装置のクリーニング方法。
(1) A reactive cleaning gas that is not ion-activated is flowed into the reactor of the vapor phase growth apparatus and the exhaust pipe connected to the reactor to remove reaction products attached to the inner surfaces of the reactor and the exhaust pipe. A method for cleaning a vapor phase growth apparatus, characterized by removing.
(2)リアクタと、該リアクタに接続されている排気管
と、該排気管に接続されている原料ガス用廃ガス処理部
とを備えた気相成長装置のクリーニング装置において、
前記リアクタ内に開閉バルブを介してイオン活性化され
ていない反応性クリーニングガスを供給する反応性クリ
ーニングガス供給配管と、前記原料ガス用廃ガス処理部
とは別に前記排気管に反応性クリーニングガス排気管を
介して接続されていて前記反応性クリーニングガスの処
理を行う反応性クリーニングガス用廃ガス処理部と、前
記原料ガス用廃ガス処理部又は前記反応性クリーニング
ガス用廃ガス処理部のいずれかを選択的に使用するため
に前記排気管と前記反応性クリーニングガス排気管とに
接続されている切替えバルブとを有することを特徴とす
る気相成長装置のクリーニング装置。
(2) A cleaning device for a vapor phase growth apparatus comprising a reactor, an exhaust pipe connected to the reactor, and a raw material gas waste gas treatment section connected to the exhaust pipe,
A reactive cleaning gas supply pipe that supplies a non-ion activated reactive cleaning gas into the reactor via an on-off valve, and a reactive cleaning gas exhaust pipe that is separate from the raw material gas waste gas treatment section. A reactive cleaning gas waste gas treatment section that is connected via a pipe and processes the reactive cleaning gas, and either the raw material gas waste gas treatment section or the reactive cleaning gas waste gas treatment section. A cleaning device for a vapor phase growth apparatus, comprising a switching valve connected to the exhaust pipe and the reactive cleaning gas exhaust pipe for selectively using the reactive cleaning gas.
JP31767589A 1989-12-08 1989-12-08 Method and apparatus for cleaning vapor growth device Pending JPH03183693A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP31767589A JPH03183693A (en) 1989-12-08 1989-12-08 Method and apparatus for cleaning vapor growth device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP31767589A JPH03183693A (en) 1989-12-08 1989-12-08 Method and apparatus for cleaning vapor growth device

Publications (1)

Publication Number Publication Date
JPH03183693A true JPH03183693A (en) 1991-08-09

Family

ID=18090769

Family Applications (1)

Application Number Title Priority Date Filing Date
JP31767589A Pending JPH03183693A (en) 1989-12-08 1989-12-08 Method and apparatus for cleaning vapor growth device

Country Status (1)

Country Link
JP (1) JPH03183693A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0799187A (en) * 1993-07-09 1995-04-11 Iwatani Internatl Corp Non-plasma cleaning method in semiconductor manufacturing equipment
JPH07283152A (en) * 1994-02-21 1995-10-27 Matsushita Electric Ind Co Ltd Semiconductor manufacturing apparatus, gas supply apparatus, exhaust gas processing apparatus, and method for opening air to pneumatic equipment
JP2002353210A (en) * 2001-05-25 2002-12-06 Tokyo Electron Ltd Heat treatment apparatus and heat treatment method
JP2003101152A (en) * 2001-09-27 2003-04-04 Ricoh Co Ltd Method for manufacturing semiconductor light emitting device, semiconductor laser manufactured using the method, and optical communication system
US7453096B2 (en) 2001-03-27 2008-11-18 Ricoh Company, Ltd. Method of fabricating a semiconductor light-emitting device
US7518161B2 (en) 2001-03-27 2009-04-14 Ricoh Company, Ltd. Semiconductor light-emitting device, surface-emission laser diode, and production apparatus thereof, production method, optical module and optical telecommunication system
US7968362B2 (en) 2001-03-27 2011-06-28 Ricoh Company, Ltd. Semiconductor light-emitting device, surface-emission laser diode, and production apparatus thereof, production method, optical module and optical telecommunication system
JP2023022938A (en) * 2021-08-04 2023-02-16 東京エレクトロン株式会社 Substrate water vapor processing method and substrate water vapor processing system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0799187A (en) * 1993-07-09 1995-04-11 Iwatani Internatl Corp Non-plasma cleaning method in semiconductor manufacturing equipment
JPH07283152A (en) * 1994-02-21 1995-10-27 Matsushita Electric Ind Co Ltd Semiconductor manufacturing apparatus, gas supply apparatus, exhaust gas processing apparatus, and method for opening air to pneumatic equipment
US7453096B2 (en) 2001-03-27 2008-11-18 Ricoh Company, Ltd. Method of fabricating a semiconductor light-emitting device
US7518161B2 (en) 2001-03-27 2009-04-14 Ricoh Company, Ltd. Semiconductor light-emitting device, surface-emission laser diode, and production apparatus thereof, production method, optical module and optical telecommunication system
US7968362B2 (en) 2001-03-27 2011-06-28 Ricoh Company, Ltd. Semiconductor light-emitting device, surface-emission laser diode, and production apparatus thereof, production method, optical module and optical telecommunication system
US8293555B2 (en) 2001-03-27 2012-10-23 Ricoh Company, Ltd. Semiconductor light-emitting device, surface-emission laser diode, and production apparatus thereof, production method, optical module and optical telecommunication system
JP2002353210A (en) * 2001-05-25 2002-12-06 Tokyo Electron Ltd Heat treatment apparatus and heat treatment method
JP2003101152A (en) * 2001-09-27 2003-04-04 Ricoh Co Ltd Method for manufacturing semiconductor light emitting device, semiconductor laser manufactured using the method, and optical communication system
JP2023022938A (en) * 2021-08-04 2023-02-16 東京エレクトロン株式会社 Substrate water vapor processing method and substrate water vapor processing system

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