JP2998181B2 - High boiling point gas recovery method - Google Patents

High boiling point gas recovery method

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Publication number
JP2998181B2
JP2998181B2 JP21863090A JP21863090A JP2998181B2 JP 2998181 B2 JP2998181 B2 JP 2998181B2 JP 21863090 A JP21863090 A JP 21863090A JP 21863090 A JP21863090 A JP 21863090A JP 2998181 B2 JP2998181 B2 JP 2998181B2
Authority
JP
Japan
Prior art keywords
gas
supply pipe
boiling
gas cylinder
exhaust
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
JP21863090A
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Japanese (ja)
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JPH04103766A (en
Inventor
敏明 古舘
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Fujitsu Ltd
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Fujitsu Ltd
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Publication of JPH04103766A publication Critical patent/JPH04103766A/en
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Description

【発明の詳細な説明】 〔概要〕 本発明は,毒性,腐食性,或いは可燃性のガスをメン
テナンス等により不活ガスに置換する必要があるガスの
回収方法に係わり,特に,常温で蒸気圧の低い高沸点ガ
スの回収方法に関し, 安全,迅速,かつ確実に回収することを目的とし, 成膜,或いはエッチング等に使用する半導体製造装置
に,高沸点ガスのガスシリンダーより,該高沸点ガスを
送り込む供給配管内の該高沸点ガスを除去するに際し,
該ガスシリンダーを該供給配管内の温度より低い温度に
冷却して回収するように構成する。
DETAILED DESCRIPTION OF THE INVENTION [Summary] The present invention relates to a method for recovering a gas that needs to be replaced with an inert gas by maintenance or the like for a toxic, corrosive, or flammable gas. For the method of recovering high-boiling gas with low boiling point, for the purpose of safe, rapid and reliable recovery, semiconductor manufacturing equipment used for film formation or etching, etc. When removing the high-boiling gas in the supply pipe for feeding
The gas cylinder is configured to be cooled and recovered to a temperature lower than the temperature in the supply pipe.

〔産業上の利用分野〕[Industrial applications]

本発明は,毒性,腐食性,或いは可燃性のガスをメン
テナンス等により不活性ガスに置換する必要があるガス
の回収方法に係わり,特に,常温で蒸気圧の低い高沸点
ガスの回収方法に関する。
The present invention relates to a method for recovering a gas that requires replacement of a toxic, corrosive or flammable gas with an inert gas for maintenance or the like, and more particularly to a method for recovering a high boiling point gas having a low vapor pressure at room temperature.

近年の集積回路半導体装置の技術的進歩は目覚まし
く,それに伴いウエハープロセスにおいて,各種の高圧
ガスが金属,半導体,絶縁膜等の成膜装置或いはエッチ
ング装置に用いられている。
In recent years, the technical progress of integrated circuit semiconductor devices has been remarkable, and accordingly, in a wafer process, various high-pressure gases have been used in film forming apparatuses for metal, semiconductor, insulating films and the like or in etching apparatuses.

この中には,毒性,腐食性,或いは可燃性のガスも多
く用いられ,装置の改良,故障,メンテナンス(保全)
等により装置内或いは供給配管内を窒素等の不活性ガス
に置換する必要が度々生ずる。
Among them, many toxic, corrosive or flammable gases are used, so equipment improvement, breakdown, maintenance (maintenance)
For example, it is often necessary to replace the inside of the apparatus or the supply pipe with an inert gas such as nitrogen.

そのため,安全,迅速,かつ確実に回収する方法の開
発が必要となってくる。
For this reason, it is necessary to develop a safe, quick, and reliable method of recovery.

〔従来の技術〕[Conventional technology]

第3図は従来例の説明図である。 FIG. 3 is an explanatory view of a conventional example.

図において,21は半導体製造装置,22はガスシリンダ
ー,23は供給配管,24は排気配管,25はバイパス排気配管,
26は排気処理装置,27はスクラバー,28は不活性ガスであ
る。
In the figure, 21 is a semiconductor manufacturing apparatus, 22 is a gas cylinder, 23 is a supply pipe, 24 is an exhaust pipe, 25 is a bypass exhaust pipe,
26 is an exhaust gas treatment device, 27 is a scrubber, and 28 is an inert gas.

半導体装置の製造の際,ウエハープロセスにおいて,
毒性,腐食性,或いは,可燃性の各種の高圧ガスが金
属,半導体,絶縁膜等の成膜装置或いはエッチング装置
に用いられている。後えば,成膜の化学的気相成長装置
では,トリクロルシラン(SiHCl3),六弗化タングステ
ン(WF6),等が用いられ,エッチング装置では,四塩
化珪素(SiCl4),三塩化硼素(BCl3)等が多く用いら
れている。
In the manufacture of semiconductor devices, in the wafer process,
Various toxic, corrosive, or combustible high-pressure gases are used in film-forming apparatuses or etching apparatuses for metal, semiconductor, insulating films, and the like. Later, trichlorosilane (SiHCl 3 ), tungsten hexafluoride (WF 6 ), etc. are used in a chemical vapor deposition apparatus for film formation, and silicon tetrachloride (SiCl 4 ) and boron trichloride are used in an etching apparatus. (BCl 3 ) and the like are often used.

これらのガスの有害性に対処するために,定期的にリ
ークチエックを行い,また,半導体材料ガスとして,常
に高純度を要求されることから,長期間装置を使用する
場合には,ドライでクリーンな不活性ガスによる定期的
なリフレッシュが必要となる。
In order to deal with the harmfulness of these gases, a leak check should be performed periodically, and since high purity is always required as a semiconductor material gas, dry and clean Periodic refresh with an inert gas is required.

このため,メンテナンス実施の際には,毒性,可燃
性,或いは,腐食性のガスをあらかじめ配管系内から排
除し,人的,設備的に安全な状態にする必要がある。
For this reason, when performing maintenance, it is necessary to remove toxic, flammable, or corrosive gases from the piping system in advance, and to maintain a safe state for humans and equipment.

従来技術においては,配管内の高沸点ガス等を不活性
ガスに置換する工程に際して,高沸点ガス等の実ガスを
抜く方法としては,第3図に示すような排気処理システ
ムを使用していた。
In the prior art, an exhaust treatment system as shown in FIG. 3 was used as a method for extracting a high-boiling gas or the like in the process of replacing a high-boiling gas or the like in a pipe with an inert gas. .

実ガスの供給配管23の長さは,半導体装置21からスク
ラバー27迄の排気配管24の長さに比べて,はるかに長
く,不活性ガスとして窒素を不活性ガス導入口28から送
り込み,供給配管23から半導体装置21,排気配管24,排気
処理装置26,スクラバー27を経由して高沸点ガスを排出
していた。
The length of the supply pipe 23 for the actual gas is much longer than the length of the exhaust pipe 24 from the semiconductor device 21 to the scrubber 27. Nitrogen is supplied as an inert gas from the inert gas inlet 28 and supplied to the supply pipe. The high-boiling gas was discharged from 23 through the semiconductor device 21, the exhaust pipe 24, the exhaust processing device 26, and the scrubber 27.

ところが,高沸点ガスは蒸気圧がゲージ圧力で0〜1.
5kg/cm2,或いはそれ以下と低く,実際のガスは供給圧力
=蒸気圧といった状態で供給しているために,供給径路
に温度むらがある場合には,蒸気圧に勾配が生じて,低
圧部分で飽和状態となり,再液化してしまう。このた
め,実ガスを抜く工程に多くの工数やコストを要してい
た。
However, for high-boiling gas, the vapor pressure is 0 to 1.
5 kg / cm 2 or lower, and the actual gas is supplied under the condition of supply pressure = vapor pressure. If there is uneven temperature in the supply path, a gradient will occur in the vapor pressure and low pressure The part becomes saturated and re-liquefies. For this reason, a lot of man-hours and costs were required for the process of extracting the actual gas.

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

従って,従来の排気処理装置を使用したガス置換方法
では下記のような問題点を生ずる。
Therefore, the following problems occur in the gas replacement method using the conventional exhaust treatment device.

即ち, 供給配管系内には,周囲温度のむらに起因する多量
のガスの再液化現象が生じるために,ガスの供給配管内
の再液化したガスを気化して抜くためのガス置換作業
に,工数と時間が掛かる。
In other words, since a large amount of gas re-liquefaction occurs due to uneven ambient temperature in the supply piping system, man-hours are required for gas replacement work for vaporizing and removing the re-liquefied gas in the gas supply piping. It takes time.

排気処理系において再液化現象が生じるために,ガ
ス置換の処理時間が一定しない。また,故障した際の改
修作業で多量のガスが発生して,人体に危険が伴う。
Since the reliquefaction phenomenon occurs in the exhaust processing system, the processing time of the gas replacement is not constant. In addition, a large amount of gas is generated during the repair work in the event of a breakdown, which is dangerous to the human body.

排気処理系において,不活性ガス置換工程の場合に
は,エッチングや成膜工程とは別の状態,即ち,廃棄処
理系を通過するガスの流量が数倍も多くなり,対象ガス
の反応生成物が急成長して配管内に蓄積し,排気処理装
置,特にポンプが詰まる等の故障が多発する。
In the case of the exhaust gas treatment system, in the case of the inert gas replacement process, the flow rate of the gas passing through the waste treatment system is several times larger than that of the etching or film formation process, that is, the reaction product of the target gas is increased. Rapidly grows and accumulates in the piping, causing many failures such as clogging of exhaust treatment devices, especially pumps.

排気処理系において,乾式除害剤を使用する場合
に,乾式除害剤の使用量が多くなり,ランニングコスト
が高くなり,稼働率が低下する。
In the case of using a dry abatement agent in an exhaust treatment system, the use amount of the dry abatement agent increases, the running cost increases, and the operation rate decreases.

再液化したガスは廃棄することとなり,ガスの消費
量が多くなる。
The reliquefied gas will be discarded, and the gas consumption will increase.

本発明は,以上の点に鑑み,半導体装置への高沸点ガ
スの供給配管内におけるガスの回収作業において,安
全,迅速,かつ確実に高沸点ガスが回収できる方法を得
ることを目的として提供されるものである。
The present invention has been made in view of the above circumstances, and has as its object to provide a method for recovering a high-boiling gas safely, quickly, and reliably in a gas recovery operation in a supply pipe of a high-boiling gas to a semiconductor device. Things.

〔課題を解決するための手段〕[Means for solving the problem]

第1図は本発明の原理説明図兼一実施例の構成図,第
2図は本発明の水冷ジャケットである。
FIG. 1 is a diagram illustrating the principle of the present invention and a configuration diagram of an embodiment, and FIG. 2 is a water cooling jacket of the present invention.

図において,1は半導体製造装置,2はガスシリンダー,3
は供給配管,4は排気配管,5はバイパス排気配管,6は排気
処理装置,7はスクラバ,8は不活性ガス,9は水冷ジャケッ
ト,10は冷却水温度調節器である。
In the figure, 1 is a semiconductor manufacturing equipment, 2 is a gas cylinder, 3
Is a supply pipe, 4 is an exhaust pipe, 5 is a bypass exhaust pipe, 6 is an exhaust treatment device, 7 is a scrubber, 8 is an inert gas, 9 is a water cooling jacket, and 10 is a cooling water temperature controller.

前記のように,従来の技術では,排気処理システムを
用いるために,蒸気圧の低いガスでは圧力むらのため,
再液化を生じて,この排除に多大の労力,時間,費用が
かかる。
As described above, in the conventional technology, the exhaust treatment system is used, and the gas having a low vapor pressure has uneven pressure.
Re-liquefaction takes place and this elimination requires a great deal of labor, time and money.

このため,本発明では,当該ガスシリンダー2そのも
のを周囲温度より低い温度に冷却して,ガスシリンダー
2内部のガス蒸気圧を低く保ち,供給配管3内のガス蒸
気圧との間に圧力勾配を生じさせる。
For this reason, in the present invention, the gas cylinder 2 itself is cooled to a temperature lower than the ambient temperature, the gas vapor pressure inside the gas cylinder 2 is kept low, and a pressure gradient is formed between the gas cylinder 2 and the supply pipe 3. Cause.

このことにより,ガスは高圧側である供給配管3よ
り,低圧側のガスシリンダー2へ逆流して回収されるた
めに,供給配管3内のガスを抜くことが可能となる。
Thereby, the gas flows backward from the supply pipe 3 on the high pressure side to the gas cylinder 2 on the low pressure side and is collected, so that the gas in the supply pipe 3 can be discharged.

即ち,本発明の目的は,成膜,或いはエッチング等に
使用する半導体製造装置1に,高沸点ガスのガスシリン
ダー2より,該高沸点ガスを送り込む供給配管3内の該
高沸点ガスを除去するに際し, 該ガスシリンダー2を該供給配管3内の温度より低い
温度に冷却して回収することにより達成される。
That is, an object of the present invention is to remove a high-boiling gas from a supply pipe 3 for feeding the high-boiling gas from a gas cylinder 2 of a high-boiling gas to a semiconductor manufacturing apparatus 1 used for film formation or etching. This is achieved by cooling and recovering the gas cylinder 2 to a temperature lower than the temperature in the supply pipe 3.

〔作用〕[Action]

上記のような構成にすることにより,本発明では,供
給配管内の温度むらに関係なく,常にガスシリンダー内
の蒸気圧が供給配管内よりも低くなる。
With the above configuration, in the present invention, the vapor pressure in the gas cylinder is always lower than that in the supply pipe regardless of the temperature unevenness in the supply pipe.

これによって,ガスは相対的に高い蒸気圧の供給配管
より,低圧側のガスシリンダー内に逆流して回収され,
結果として,供給配管内よりガスを抜くことが可能とな
る。
As a result, the gas flows back into the gas cylinder on the low pressure side from the supply pipe with a relatively high vapor pressure, and is collected.
As a result, gas can be released from the supply pipe.

〔実施例〕〔Example〕

第1図は本発明の一実施例の構成図,第2図は本発明
の一実施例に使用した水冷ジャケットである。
FIG. 1 is a configuration diagram of one embodiment of the present invention, and FIG. 2 is a water cooling jacket used in one embodiment of the present invention.

図において,1は半導体製造装置,2はガスシリンダー,3
は供給配管,4は排気配管,5はバイパス排気配管,6は排気
処理装置,7はスクラバ,8は不活性ガス,9は水冷ジャケッ
ト,10は冷却水温度調節器,11はベース,12は水冷管,13は
供給口,14は排出口,15は断熱材,16はクランプベルトで
ある。
In the figure, 1 is a semiconductor manufacturing equipment, 2 is a gas cylinder, 3
Is a supply pipe, 4 is an exhaust pipe, 5 is a bypass exhaust pipe, 6 is an exhaust treatment device, 7 is a scrubber, 8 is an inert gas, 9 is a water cooling jacket, 10 is a cooling water temperature controller, 11 is a base, and 12 is A water cooling tube, 13 is a supply port, 14 is a discharge port, 15 is a heat insulating material, and 16 is a clamp belt.

第1図に示すように,成膜,或いはエッチング等に使
用する半導体製造装置1に,高沸点ガスのガスシリンダ
ー2より,高沸点ガスを半導体製造装置1に供給する供
給配管3内の高沸点ガスを除去するに際し,供給する高
沸点ガスのガスシリンダー2を供給配管3内の温度より
低い温度に冷却して回収する。
As shown in FIG. 1, a high-boiling gas in a supply pipe 3 for supplying a high-boiling gas from a gas cylinder 2 of a high-boiling gas to a semiconductor manufacturing apparatus 1 used for film formation or etching. In removing the gas, the supplied high-boiling-point gas cylinder 2 is cooled to a temperature lower than the temperature in the supply pipe 3 and recovered.

この,ガスシリンダー2を冷却する方法の第1の実施
例としては,第2図に示すように,水冷ジャケットを用
いる。
As a first embodiment of the method for cooling the gas cylinder 2, a water cooling jacket is used as shown in FIG.

水冷ジャケットは第2図に示すように,内側には,ガ
スシリンダー2の側面を包むための銅製の厚さ2mmの二
つ折りの円筒からなるベース11を使用し,その外側に熱
交換パイプとして10mm径の銅製の水冷管12をジグザグに
溶接してある。
As shown in Fig. 2, the water-cooled jacket uses a copper-made base 2 consisting of a 2-fold copper cylinder with a thickness of 2 mm for wrapping the sides of the gas cylinder 2 and a heat-exchange pipe with a diameter of 10 mm on the outside. The copper water cooling tube 12 is welded zigzag.

そして,この水冷管12の供給口13より約5℃の冷水を
導入し,排出口14より排出する。
Then, cold water of about 5 ° C. is introduced from the supply port 13 of the water cooling pipe 12 and discharged from the discharge port 14.

水冷管の外側に断熱材15を巻き,クランプベルト16で
止める。
A heat insulating material 15 is wound around the outside of the water cooling tube, and is stopped with a clamp belt 16.

本発明の装置を用いてガスシリンダーを冷却した場合
の,高沸点ガスの蒸気圧の一例を次表に示す。
The following table shows an example of the vapor pressure of a high-boiling gas when the gas cylinder is cooled using the apparatus of the present invention.

上記の表で見られるように,室温に対して10〜20℃の
ガスシリンダー2の冷却を行えば,ガスシリンダー2と
供給配管3との温度差にもとずく蒸気圧の差により,供
給配管内の高沸点ガスはガスシリンダー内に殆ど回収さ
れる。
As can be seen from the above table, if the gas cylinder 2 is cooled to 10 to 20 ° C. with respect to the room temperature, the difference in steam pressure based on the temperature difference between the gas cylinder 2 and the supply pipe 3 causes the supply pipe to be cooled. Most of the high-boiling gas inside is recovered in the gas cylinder.

この方法は,メンテナンス時の荒引き(1次排気)に
適用され,これによって供給配管3内の高沸点ガスは殆
どガスシリンダー2内に回収される。
This method is applied to rough evacuation (primary exhaust) at the time of maintenance, whereby most of the high-boiling gas in the supply pipe 3 is recovered in the gas cylinder 2.

この後,半導体装置と供給配管の間のバルブを開い
て,微小な残留ガスの2次排気を行う。
Thereafter, the valve between the semiconductor device and the supply pipe is opened to perform secondary exhaust of minute residual gas.

尚,ガスシリンダー2を冷却する第2の実施例として
は,ガスシリンダー2を氷水或いは塩水を満たしたジャ
ーに浸漬する方法があり,第3の実施例としては,ガス
シリンダー2に冷風を吹き掛ける方法も可能である。
As a second embodiment for cooling the gas cylinder 2, there is a method of immersing the gas cylinder 2 in a jar filled with ice water or salt water. As a third embodiment, cool air is blown on the gas cylinder 2. A method is also possible.

〔発明の効果〕〔The invention's effect〕

本発明によれば,下記に列記したような効果が挙が
る。
According to the present invention, the following effects can be obtained.

ガス置換作業工数の短縮と安定化。Shortening and stabilizing gas replacement work.

排気処理設備の負荷低減及びコストダウン, 排気処理装置の故障に伴う不安全性の回避。Reduce load and cost of exhaust treatment equipment, and avoid unsafety due to failure of exhaust treatment equipment.

再液化ガス回収によるガスの有効利用。Effective use of gas by reliquefied gas recovery.

排気処理作業の減少に伴う安全性の向上。Improved safety due to reduced exhaust treatment work.

以上のように,回収作業の工数や費用が削減され,安
全性の向上に寄与するところが大きい。
As described above, the man-hour and cost of the collection work are reduced, which greatly contributes to the improvement of safety.

【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の構成図, 第2図は本発明の一実施例に使用した水冷ジャケット, 第3図は従来例の説明図 である。 図において, 1は半導体製造装置,2はガスシリンダー, 3は供給配管,4は排気配管, 5はバイパス排気配管, 6は排気処理装置,7はスクラバ, 8は不活性ガス,9は水冷ジャケット, 10は冷却水温度調節器, 11はベース,12は水冷管, 13は供給口,14は排出口, 15は断熱材,16はクランプベルト である。 FIG. 1 is a block diagram of one embodiment of the present invention, FIG. 2 is a water cooling jacket used in one embodiment of the present invention, and FIG. 3 is an explanatory diagram of a conventional example. In the figure, 1 is a semiconductor manufacturing apparatus, 2 is a gas cylinder, 3 is a supply pipe, 4 is an exhaust pipe, 5 is a bypass exhaust pipe, 6 is an exhaust processing apparatus, 7 is a scrubber, 8 is an inert gas, and 9 is a water cooling jacket. , 10 is a cooling water temperature controller, 11 is a base, 12 is a water cooling tube, 13 is a supply port, 14 is a discharge port, 15 is a heat insulating material, and 16 is a clamp belt.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】半導体製造装置に、常温付近に沸点を有
し、常温で蒸気圧の低い高沸点ガスのガスシリンダーよ
り、前記高沸点ガスを送り込む供給配管内の前記高沸点
ガスを除去するに際し、 前記高沸点ガスの前記ガスシリンダー内を前記供給配管
内の温度よりも低い温度に冷却することにより、前記供
給配管内の前記高沸点ガスを前記ガスシリンダーに回収
することを特徴とする高沸点ガス回収方法。
1. A method for removing a high-boiling gas in a supply pipe for feeding the high-boiling gas from a gas cylinder of a high-boiling gas having a boiling point near room temperature and having a low vapor pressure at room temperature in a semiconductor manufacturing apparatus. Cooling the inside of the gas cylinder of the high-boiling gas to a temperature lower than the temperature of the supply pipe, thereby recovering the high-boiling gas in the supply pipe to the gas cylinder. Gas recovery method.
JP21863090A 1990-08-20 1990-08-20 High boiling point gas recovery method Expired - Fee Related JP2998181B2 (en)

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Application Number Priority Date Filing Date Title
JP21863090A JP2998181B2 (en) 1990-08-20 1990-08-20 High boiling point gas recovery method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21863090A JP2998181B2 (en) 1990-08-20 1990-08-20 High boiling point gas recovery method

Publications (2)

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JPH04103766A JPH04103766A (en) 1992-04-06
JP2998181B2 true JP2998181B2 (en) 2000-01-11

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JPH04103766A (en) 1992-04-06

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