JPH01281131A - Method and apparatus for treating exhaust gas generated from semiconductor production process - Google Patents

Method and apparatus for treating exhaust gas generated from semiconductor production process

Info

Publication number
JPH01281131A
JPH01281131A JP63238854A JP23885488A JPH01281131A JP H01281131 A JPH01281131 A JP H01281131A JP 63238854 A JP63238854 A JP 63238854A JP 23885488 A JP23885488 A JP 23885488A JP H01281131 A JPH01281131 A JP H01281131A
Authority
JP
Japan
Prior art keywords
exhaust gas
absorbent
semiconductor manufacturing
reaction chamber
bypass valve
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.)
Granted
Application number
JP63238854A
Other languages
Japanese (ja)
Other versions
JPH0461686B2 (en
Inventor
Akira Fukunaga
明 福永
Manabu Tsujimura
学 辻村
Masaaki Osato
大里 雅昭
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.)
Ebara Corp
Ebara Research Co Ltd
Original Assignee
Ebara Corp
Ebara Research Co Ltd
Ebara Infilco 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 Ebara Corp, Ebara Research Co Ltd, Ebara Infilco Co Ltd filed Critical Ebara Corp
Priority to JP63238854A priority Critical patent/JPH01281131A/en
Publication of JPH01281131A publication Critical patent/JPH01281131A/en
Publication of JPH0461686B2 publication Critical patent/JPH0461686B2/ja
Granted legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Gas Separation By Absorption (AREA)

Abstract

PURPOSE:To prevent large fluctuation of flow rate by arranging a bypass piping between an inlet and outlet pipings of an absorbentpacked vessel so that an exhaust gas during an evacuation of a reaction chamber is allowed to bypass the absorbent-packed vessel and not to flow into it. CONSTITUTION:A process gas 1 is introduced into a highly evacuated reaction chamber 14 for semiconductor production, reacts with wafers, and an exhaust gas is pumped out by an exhaust equipment 5, sent to a dry absorbent-packed vessel 10 and treated to become harmless. An exhaust gas while evacuating the reaction chamber 14 after it has been returned to atmospheric pressure for the purpose of maintenance, etc., is ejected through a bypass piping 8 by opening a bypass valve 7. An exhaust gas remaining in the bypass piping 8 is replaced by purging it with an inert gas introduced through a piping 8 and sending it to the absorbent-packed vessel 10.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は半導体製造排ガスの処理方法及びその装置に係
シ、特に乾式吸収剤によって処理するのに好適な処理方
法及びその製造に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method and apparatus for treating exhaust gas from semiconductor manufacturing, and particularly to a treatment method suitable for treatment with a dry absorbent and its production.

〔従来の技術〕[Conventional technology]

半導体製造工程ではプラズマCVDやプラズマエツチン
グなどドライプロセスの採用が進んでお夕、これにとも
なって排ガス処理の必要性が高まってきている。特に最
近では、簡便性その他の点から乾式法による排ガス処理
に対する期待が強くなり、種々のガスに応じ九吸収剤が
実用に供されている。
As dry processes such as plasma CVD and plasma etching are increasingly adopted in semiconductor manufacturing processes, the need for exhaust gas treatment is increasing. Particularly in recent years, there have been strong expectations for exhaust gas treatment by the dry method due to its simplicity and other reasons, and nine absorbents have been put into practical use for various gases.

ところで、上記のプロセスのガス排出量について詳しく
検討してみると、ウェハ処理中に排出されるガス量は使
用するガスの合計流量にほぼ等しく毎分数を前後である
のに対して、反応室を大気圧から真空引きする際には排
気ポンプの定格排気量に相当する毎分数千tのガスが短
時間ではあるが排気されることKなる。
By the way, if we examine the amount of gas emitted in the above process in detail, we find that the amount of gas emitted during wafer processing is approximately equal to the total flow rate of the gases used, which is approximately several times per minute. When evacuation is performed from atmospheric pressure, several thousand tons of gas are exhausted per minute, which corresponds to the rated displacement of the exhaust pump, albeit for a short period of time.

半導体製造装置からの排ガスをそのまま乾式吸収剤で処
理する場合には、このようなきわめて大幅な流量変動に
対しても安定にかつ安全に処理できるような吸収剤を使
う必要がある。即ち、大流量の排ガスを吸収剤の充てん
層に通した場合にも1通気抵抗がほとんど現われず、し
かも充てん層内で被処理ガス成分を完全に吸収できるよ
うな吸収剤を使わなければならない。
When exhaust gas from semiconductor manufacturing equipment is treated directly with a dry absorbent, it is necessary to use an absorbent that can be treated stably and safely even with such extremely large fluctuations in flow rate. That is, it is necessary to use an absorbent that exhibits almost no ventilation resistance even when a large flow of exhaust gas is passed through a packed layer of absorbent, and that can completely absorb the components of the gas to be treated within the filled layer.

しかしながら、一般に通気抵抗を低く保つためには粗大
な吸収剤を使わざるを得ないが、粒径が大きくなると吸
収ないし吸着に関与する表面積が相対的に小さくなシ吸
収Stの低下を免かれない。そのため多孔性の吸収剤を
使って吸収G tの向上を計るなどの試みがなされてい
るが、これらの方法にも限界があシ、結局吸収剤を相当
被充てんすることによυ所定の吸収容量を確保している
のが実状でめる。また、排ガスによっては吸収剤と反応
して固形物を生成するものもあり、そのような場合には
、吸収剤を粗大にしておいても、反応生成物によって徐
々に充てん層が閉塞されてゆくので通気抵抗の上昇をま
ぬがれることかできない。
However, in general, coarse absorbents have to be used in order to keep airflow resistance low, but as the particle size increases, the surface area involved in absorption or adsorption is relatively small, resulting in a decrease in absorption St. . For this reason, attempts have been made to improve the absorption Gt using porous absorbents, but these methods also have their limits, and in the end, it is necessary to fill the absorbent with a considerable amount to achieve the desired absorption Gt. The reality is that we have secured capacity. Additionally, some exhaust gases react with the absorbent to form solids, and in such cases, even if the absorbent is coarsened, the reaction products will gradually block the packed layer. Therefore, it is impossible to avoid an increase in ventilation resistance.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

本発明は、半導体製造装置からの排ガスを乾式吸収剤で
処理する際の排ガスの大幅な流量変動を回避し、より小
粒径の吸収剤を使っても安全かつ効率的に処理し得る方
法及びその装置を提供するものである。
The present invention provides a method and a method that can avoid large fluctuations in the flow rate of exhaust gas when treating exhaust gas from semiconductor manufacturing equipment with a dry absorbent, and can safely and efficiently process the exhaust gas even when using an absorbent with a smaller particle size. The present invention provides such equipment.

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

本発明は半導体製造装置からの排ガスを乾式吸収剤によ
って処理する方法において、吸収剤充てん容器の入口側
配管と出口側配管の間にバイパス弁を備えたバイパス配
管を設け、半導体製造装置の反応室を大気圧から排気す
る際に生ずる大量の排気をバイパス弁を開けることによ
り吸収剤充てん容器に導入しないようにすると共に、バ
イパス管以前の排気系内に滞留している被処理ガスを前
もって不活性ガスにより置換させておくことを特徴とす
るものである。
The present invention provides a method for treating exhaust gas from semiconductor manufacturing equipment with a dry absorbent, in which a bypass pipe equipped with a bypass valve is provided between an inlet side pipe and an outlet side pipe of an absorbent-filled container, and the reaction chamber of the semiconductor manufacturing equipment is By opening the bypass valve, a large amount of exhaust gas generated when exhausting gas from atmospheric pressure is prevented from being introduced into the absorbent-filled container, and the gas to be treated that remains in the exhaust system before the bypass pipe is inertized in advance. It is characterized in that it is replaced with gas.

〔実施例1〕 本発明につき、一実施例を図面を参照しながら詳述する
[Example 1] An example of the present invention will be described in detail with reference to the drawings.

第1図は、半導体製造装置から排ガス吸収剤充てん容器
に至るフローを模式的に示したものである。
FIG. 1 schematically shows the flow from the semiconductor manufacturing equipment to the exhaust gas absorbent filling container.

半導体製造装置2はプラズマCVDやプラズマエツチン
グ等の高真空下でウェハを処理するものであれば形式を
問わず、従ってまたプロセスガス1の種類や流量もそれ
ぞれのグロセス〈応じたもののいずれであってもよい。
The semiconductor manufacturing equipment 2 may be of any type as long as it processes wafers under high vacuum such as plasma CVD or plasma etching, and therefore the type and flow rate of the process gas 1 may vary depending on the respective gross process. Good too.

また、吸収剤充てん容器10に充てんすべき吸収剤の種
類とその充てん量及び充てん容器の寸法・形状も、それ
ぞれの排ガスに応じて公知のものを採用できる。
Further, the type and amount of absorbent to be filled in the absorbent filling container 10, and the dimensions and shape of the filling container can be selected from known ones depending on each exhaust gas.

一般にウェハ処理中には、プロセスガス1は半導体製造
装置の反応室14に導入されてウェハと反応し、反応後
の排ガスは排気装置5により排気されて吸収剤充てん容
器に送られ、無害化された後に排出される。
Generally, during wafer processing, process gas 1 is introduced into the reaction chamber 14 of semiconductor manufacturing equipment and reacts with the wafer, and the exhaust gas after the reaction is exhausted by the exhaust device 5 and sent to an absorbent-filled container to be rendered harmless. It is then discharged.

また、ウェハ交換やメンテナンスのために半導体製造装
置の反応室i4を大気圧に戻した後に再度排気装置5に
よって真空引きする際の大量の排気は、バイパス弁7を
開放してバイパス配管8により吸収剤充てん容器10を
通すことなく排出する。この際、大量の排気はメインパ
ルプ5が開いて始めて吐出されるものであるので、バイ
パス弁7の開放はメインパルプ5を開放する為の信号に
基いて事前に行なっておけばよい。ただし、メインパル
プ3はエツチング中も開いたtまであるので、そのまま
ではバイパス弁7も開いたままとなる。そこでタイマに
より所定時間後に閉じるようにするが、その際のタイマ
設定時間は、排気流量が低下して吸収剤充てん容器10
0入口圧力が低くなるのに充分な時間であって、しかも
反応室内にプロセスガスが導入される以前の任意の時間
で良い。
In addition, when the reaction chamber i4 of the semiconductor manufacturing equipment is returned to atmospheric pressure for wafer exchange or maintenance and then evacuated again by the exhaust device 5, a large amount of exhaust gas is absorbed by the bypass piping 8 by opening the bypass valve 7. The agent is discharged without passing through the agent filling container 10. At this time, since a large amount of exhaust gas is discharged only after the main pulp 5 is opened, the bypass valve 7 may be opened in advance based on a signal for opening the main pulp 5. However, since the main pulp 3 remains open up to t during etching, the bypass valve 7 also remains open. Therefore, a timer is set to close after a predetermined time, but the timer setting time at that time is such that the exhaust flow rate decreases and the absorbent filling container 10 closes.
The time may be any time sufficient for the zero inlet pressure to decrease and before the process gas is introduced into the reaction chamber.

ま九、大量の排気をそのまま吸収剤充てん容器に導入す
ると、容器入口側の圧力が上昇するので、この圧力上昇
を圧力検知器9により感知し、その信号によりバイパス
弁7を開としてもよい。ただしこの場合にはバイパス弁
7か開ぐと同時に入口圧力が低下し、それを圧力検知器
9が感知してバイパス弁を閉じてしまい、再度圧力が上
昇してバイパス弁が開くというよ5なハンチング現象が
起こる可能性がある。そこでやはシタイiを使用し、排
気流量が少なくなりバイパス弁を閉じても入口圧力が充
分低くバイパス弁が再度開くようなことがなくなる迄排
気させてからバイパス弁を閉じるよりタイマの時間を設
定すれば良い。
(9) If a large amount of exhaust gas is directly introduced into the absorbent-filled container, the pressure on the inlet side of the container will increase, so this pressure increase may be detected by the pressure detector 9, and the bypass valve 7 may be opened in response to the signal. However, in this case, the inlet pressure will drop at the same time as the bypass valve 7 opens, the pressure detector 9 will sense this and close the bypass valve, and the pressure will rise again and the bypass valve will open. A hunting phenomenon may occur. Therefore, it is better to use Shitai-i and set the timer time to exhaust air until the exhaust flow rate decreases and the inlet pressure is low enough that the bypass valve will not open again even if the bypass valve is closed, and then close the bypass valve. Just do it.

また、ウェハ処理終了直後の排気装置5から吸収剤充て
ん容器に至る排気配管4には排ガスが滞留しているので
、そのままの状態で大量の排気をバイパス弁を経由して
排出してしまうと、処理すべき排ガスが一部ではあるが
未処理のままで放出されるといり事態が生じる。従って
反応室14を排気する迄に配管に存在している排ガスを
配管6を経て導入される不活性ガスによりパージして吸
収剤充てん容器10に送りこみ、しかるのちにバイパス
弁を開放して大量の排気を放出することが好ましい。
In addition, since exhaust gas remains in the exhaust pipe 4 from the exhaust device 5 to the absorbent filling container immediately after wafer processing is completed, if a large amount of exhaust gas is discharged via the bypass valve, A situation arises in which a portion of the exhaust gas that should be treated is released untreated. Therefore, until the reaction chamber 14 is evacuated, the exhaust gas existing in the piping is purged with an inert gas introduced through the piping 6 and sent to the absorbent filling container 10, and then the bypass valve is opened to generate a large amount of gas. It is preferable to release the exhaust gas.

この際パージ用の不活性ガスは排気装置5内にないしは
その直後の適当な個所から注入すれば良く、ま念注入の
期間も常時注入ないしは反応室を排気する直前の一定期
間のみの注入のいずれでもよい。さらに注入ガスfi量
は、パージすべき配管容積、注入時間等を勘案して矢示
すれば良い。なお、排気は排気管12を経て排気される
At this time, the inert gas for purging may be injected from within the exhaust device 5 or from an appropriate location immediately after it, and the period of careful injection may be either constant injection or only for a certain period of time immediately before exhausting the reaction chamber. But that's fine. Further, the amount of injection gas fi can be determined by taking into account the volume of the pipe to be purged, the injection time, etc. Note that the exhaust gas is exhausted through the exhaust pipe 12.

〔実施例2〕 本発明をエツチング装置iK応用し九例を第2図に基い
て説明する。
[Embodiment 2] Nine examples in which the present invention is applied to an etching apparatus iK will be described with reference to FIG.

運転開始前はメインパルプ3は閉じられ、排気装置5は
常時運転されていると共に管6を経てN、ガスが常時導
入されている。そして、バイパス弁7は閉、圧力検知装
置9はopyの状態とされ、また、 Ct、用弁15−
1およびN、用弁15−2は閉とされ、反応室14は大
気圧の状態となっている。
Before the start of operation, the main pulp 3 is closed, the exhaust device 5 is constantly operated, and N and gas are constantly introduced through the pipe 6. Then, the bypass valve 7 is closed, the pressure detection device 9 is in the opy state, and the Ct, valve 15-
1 and N valves 15-2 are closed, and the reaction chamber 14 is at atmospheric pressure.

該装置の運転方法を作用と共に説明すると、(1)  
先づ反応室14内にウェハを設置し蓋を閉めて密閉する
と共にメインパルプ5を開くと反応室14の大気(20
t)が排気装置5により排気される。この際排気速度が
大であるため(例えば1200 t/min )、排気
初期は大量の大気が吸収剤充てん容器10に導かれる。
The operating method of this device is explained along with its functions: (1)
First, a wafer is placed in the reaction chamber 14, the lid is closed to seal it, and when the main pulp 5 is opened, the atmosphere of the reaction chamber 14 (20
t) is exhausted by the exhaust device 5. At this time, since the evacuation speed is high (for example, 1200 t/min), a large amount of air is introduced into the absorbent filling container 10 at the initial stage of evacuation.

吸収剤充てん容器の圧力損失は、設計流量0〜50t/
分で設計されているた袷、排気配管に初期排気i 12
0027分で排気が流入すると圧力が上昇する。
The pressure loss of the absorbent-filled container is determined by the design flow rate of 0 to 50t/
Initial exhaust to the exhaust piping, which is designed in minutes I 12
When exhaust gas flows in at 0027 minutes, the pressure increases.

(2)そこでメインパルプ5が開の信号によって前もっ
てバイパス弁7を開としておくか又は圧力上昇を圧力検
知器で検知してバイパス弁7を開とすることにより、初
期の大量排気分は主としてバイパス管6全通して排気さ
れる。
(2) Therefore, by opening the bypass valve 7 in advance in response to the open signal from the main pulp 5, or by opening the bypass valve 7 by detecting the pressure increase with a pressure detector, the initial large volume of exhaust gas is mainly bypassed. It is exhausted through the entire pipe 6.

この時、バイパスされるガスは後述の説明より明らかな
ように無害なガスである。
At this time, the bypassed gas is a harmless gas, as will be clear from the explanation below.

反応室14内の大気は数秒(1〜10秒)で希薄になる
ため、その後バイパス弁7を閉じても圧力上昇は生じな
い。
Since the atmosphere in the reaction chamber 14 becomes dilute in a few seconds (1 to 10 seconds), no pressure rise occurs even if the bypass valve 7 is closed thereafter.

(3)ついで、 Ct、開弁15−1を開として例えば
α51317分のCt、を反応室14に導入してエツチ
ング反応を行なわせる。
(3) Then, open the Ct valve 15-1 to introduce, for example, a Ct of α51317 into the reaction chamber 14 to carry out an etching reaction.

(41エツチング終了後、Ct、開弁15−1を閉とし
、N8弁用15−2を開として反応室14を例えばa 
s sty分のN2ガスにて置換した後N!用開弁3−
2を閉とする。真空の場合における気体の体積は膨張し
ているため、置換は数10秒のオーダーで完了する。
(After completing etching, Ct, close the valve 15-1, open the N8 valve 15-2, and open the reaction chamber 14, for example, a
After replacing with N2 gas for s sty, N! Opening valve 3-
2 is closed. Since the volume of gas in a vacuum is expanding, the displacement is completed in the order of several tens of seconds.

この状態ではまだ排気装置から吸着剤充てん容器までの
配管(例えば数10tの容積がある)中は大気圧である
ため大気圧のCt、ガスが残っているので、とのま\で
は次のバイパスシーケンスには移ることができない。そ
こで次のウェハを設置する間を利用して導管6より導入
される例えば51/分のN、にょシ該残留Ct、ガスを
吸収剤充てん容器1oに導きあらかじめ残留C2冨ガス
を排気しておくことにより、次の操作を開始する際無害
なガスのみをバイパスさせることができる。ついで(!
)〜(4)の工程をくシ返す。
In this state, the pipe from the exhaust device to the adsorbent filling container (for example, it has a capacity of several tens of tons) is still at atmospheric pressure, so Ct and gas at atmospheric pressure remain, so we will move on to the next bypass. Cannot move to sequence. Therefore, while the next wafer is being installed, the residual Ct and gas introduced from the conduit 6 at 51/min, for example, are introduced into the absorbent-filled container 1o, and the residual C2-rich gas is evacuated in advance. This allows only harmless gas to be bypassed when starting the next operation. Then (!
) to (4).

〔発明の作用〕[Action of the invention]

本発明の処理方法及び装置を半導体製造排ガスの乾式処
理に用いると、排ガスの大幅な流量変動を回避すること
ができ、より小粒径の吸収剤を用いても通気抵抗の上昇
を招くことなく効率的かつ安全に処理を行なうことが可
能となる。
When the treatment method and apparatus of the present invention are used for the dry treatment of semiconductor manufacturing exhaust gas, it is possible to avoid large fluctuations in the flow rate of the exhaust gas, and even when using an absorbent with a smaller particle size, there is no increase in ventilation resistance. It becomes possible to perform processing efficiently and safely.

即ち、反応室を大気圧から排気する際の大量の排気はバ
イパスにより排出されるので吸収剤充てん容器には毎分
数を程度のガスのみが導入されることになり、吸収剤の
粒径を相当細かくして表面積を増やし反応効率を上げて
も通気抵抗は小さいままですむ。従って、反応室を排気
する排気装置に与える負担も少なくなり、安全な処理が
できるようになる。
In other words, a large amount of exhaust gas when the reaction chamber is evacuated from atmospheric pressure is discharged by bypass, so only a few gases are introduced into the absorbent-filled container every minute, and the particle size of the absorbent can be reduced by a considerable amount. Even if it is made finer to increase the surface area and increase the reaction efficiency, the ventilation resistance remains small. Therefore, the burden placed on the exhaust device for evacuating the reaction chamber is reduced, allowing safe processing.

また、ガス流量が低いので吸収剤との接触時間も長くと
れるようになシ、吸収剤の利用効率が大幅に向上し、一
定の処理を行なうために必要な吸収剤の量が少なくて済
み、充てん容器もコンパクトなものとすることができる
。また、排°ガスと吸収剤の反応により固形物が生成す
る場合であっても、ガス流量がきわめて少ないのでそれ
ほど大きな通気抵抗をもたらすことにはならない。
In addition, since the gas flow rate is low, the contact time with the absorbent is longer, which greatly improves the efficiency of absorbent use, and reduces the amount of absorbent required for a given process. The filling container can also be made compact. Furthermore, even if solid matter is generated by the reaction between the exhaust gas and the absorbent, the gas flow rate is extremely small, so it does not cause much ventilation resistance.

また、不活性ガスを使って常時、ないし反応室排気直前
に排気装置および配管系をパージすることKよシ処理す
べき成分を完全に吸収剤充てん容器に送り込むことがで
きるだけでなく、排気装置および配管系を常時清浄に保
つこともでき、腐食等の危険から装置全体を守ることが
可能となる。また、点検・修理等のため排気装置ないし
配管系の接続をはずすことがあるが、このような場合に
もパージを行なうことができるので危険なガスを漏出す
ることなく安全に作業を行なうことができる。
In addition, by constantly purging the exhaust system and piping system using inert gas or immediately before exhausting the reaction chamber, it is possible to not only completely send the components to be treated into the absorbent-filled container, but also to purge the exhaust system and piping system with inert gas at all times or immediately before exhausting the reaction chamber. The piping system can also be kept clean at all times, making it possible to protect the entire device from dangers such as corrosion. In addition, the exhaust system or piping system may be disconnected for inspection or repair, but in such cases, purging can be performed, allowing work to be carried out safely without leaking dangerous gases. can.

以上のように半導体製造排ガスを処理するにあ念って、
バイパス配管により反応室を大気圧から排気する際の大
量の排気を吸収剤充てん容器を通さず排出し、しかもそ
の際配管系に残存する処理すべきガス成分をあらかじめ
不活性ガスで吸収剤充てん容器までパージしておくこと
により、数多くの利点が得られる。
As mentioned above, in order to treat semiconductor manufacturing exhaust gas,
When the reaction chamber is evacuated from atmospheric pressure using bypass piping, a large amount of exhaust gas is discharged without passing through the absorbent-filled container, and at the same time, the gas components remaining in the piping system to be treated are preliminarily filled with inert gas into the absorbent-filled container. There are many benefits to purging until

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

第1図は、半導体製造装置から排ガスの吸収剤充てん容
器に至るフローを模式的に示した図、第2図は本発明を
エツチング装置に応用し九例を説明するための図である
。 1・・・プロセスガス、2・・・半導体製造装置、5・
・・メインパルプ、4・・・排気配管、5・・・排気装
置、6・−・パージガス、7・・・バイパス弁、8・・
・バイパス配管、9・・・圧力検知器、10・・・吸収
剤充てん容器、11・・・電気回路、12・・・排気管 特許出願人 株式会社荏原総会研究所 同   株式会社荏原製作所 同   荏原インフィルコ株式会社
FIG. 1 is a diagram schematically showing a flow from a semiconductor manufacturing device to a container filled with an absorbent for exhaust gas, and FIG. 2 is a diagram for explaining nine examples in which the present invention is applied to an etching device. 1... Process gas, 2... Semiconductor manufacturing equipment, 5.
... Main pulp, 4... Exhaust piping, 5... Exhaust device, 6... Purge gas, 7... Bypass valve, 8...
・Bypass piping, 9...Pressure detector, 10...Absorbent filling container, 11...Electric circuit, 12...Exhaust pipe Patent applicant Ebara General Research Institute Ebara Corporation Ebara Corporation Infilco Co., Ltd.

Claims (1)

【特許請求の範囲】 1、半導体製造装置からの排ガスを乾式吸収剤によつて
処理する如く構成した装置の反応室を、大気圧から所定
の真空度にまで排気する際に、前もつて反応室の下流側
にガス置換用不活性ガスを導入して排気装置から吸収剤
充てん室に至る排気系内に存在する被処理ガス成分を吸
収剤充てん室に送り込み、これを無害化処理して排気し
た後吸収剤充てん室の入口側配管と出口側配管との間に
設けたバイパス管を開とし反応室が所定の圧力になるま
での間の大量の排気をバイパスせしめ、吸収剤充てん室
及び排気系内の圧力上昇を回避することを特徴とする半
導体製造排ガスの処理方法。 2、反応室とこれを排気するための排気装置の間に設置
されているメインバルブを開とする信号に基いてバイパ
ス弁を開とする特許請求の範囲第1項記載の半導体製造
排ガスの処理方法。 3、吸収剤充てん容器の入口側配管上の圧力検知器によ
り入口圧力の上昇を検知し、該検知された圧力上昇信号
によりバイパス弁を開とする特許請求の範囲第1環記載
の半導体製造排ガスの処理方法。 4、半導体製造装置の反応室を大気圧から所定の圧力に
まで排気するにあたつて、前もつて半導体製造装置の排
気装置以後に、パージ用不活性ガスを常時あるいは反応
室を排気する直前に導入して排気装置から吸収剤充てん
室に至る配管内に存在する被処理ガス成分を吸収剤充て
ん容器に送り込み無害化処理する特許請求の範囲第1項
、第2項又は第3項記載の半導体製造排ガスの処理方法
。 5、半導体製造装置からの排ガスを排気する排気装置と
乾式吸収剤を充てんした吸収剤充てん容器を備えた半導
体製造排ガスの処理装置において、半導体製造装置の反
応室と前記排気装置との間にメインバルブを設け、前記
吸収剤充てん容器の入口側配管と出口側配管との間にバ
イパス弁を備えたバイパス配管を設けるとともに、前記
メインバルブ及びバイパス弁を開閉する電気回路を設け
たことを特徴とする半導体製造排ガスの処理装置。 6、前記バイパス弁が吸収剤充てん容器の入口側配管に
設けた圧力検知器の信号により開かれる特許請求の範囲
第5項記載の半導体製造排ガスの処理装置。 7、電気回路にはタイマを備え、メインバルブおよびバ
イパス弁を開放したのち、所定時間後にバイパス弁を閉
じる特許請求の範囲第5項記載の半導体製造排ガスの処
理装置。 8、電気回路にはタイマを備え、圧力検知器の信号によ
りバイパス弁を開放したのち、所定時間後に該バイパス
弁を閉じる特許請求の範囲第6項記載の半導体製造排ガ
スの処理装置。
[Claims] 1. When exhausting the reaction chamber of an apparatus configured to treat exhaust gas from semiconductor manufacturing equipment with a dry absorbent from atmospheric pressure to a predetermined degree of vacuum, An inert gas for gas replacement is introduced into the downstream side of the chamber, and the gas components to be treated that exist in the exhaust system from the exhaust device to the absorbent filling chamber are sent to the absorbent filling chamber, where they are detoxified and then exhausted. After that, the bypass pipe installed between the inlet side piping and the outlet side piping of the absorbent filling chamber is opened to bypass a large amount of exhaust gas until the reaction chamber reaches a predetermined pressure, and the absorbent filling chamber and the exhaust gas are bypassed. A method for treating semiconductor manufacturing exhaust gas characterized by avoiding a pressure increase in the system. 2. Processing of semiconductor manufacturing exhaust gas according to claim 1, in which a bypass valve is opened based on a signal to open a main valve installed between a reaction chamber and an exhaust device for exhausting the reaction chamber. Method. 3. Semiconductor manufacturing exhaust gas according to claim 1, wherein an increase in inlet pressure is detected by a pressure detector on the inlet side pipe of the absorbent-filled container, and a bypass valve is opened in response to the detected pressure increase signal. processing method. 4. When exhausting the reaction chamber of semiconductor manufacturing equipment from atmospheric pressure to a predetermined pressure, in advance, after the exhaust system of the semiconductor manufacturing equipment, inert gas for purging is constantly supplied or immediately before exhausting the reaction chamber. The method according to claim 1, 2 or 3, wherein the gas component to be treated existing in the piping from the exhaust device to the absorbent filling chamber is sent to the absorbent filling container and rendered harmless. A method for treating semiconductor manufacturing exhaust gas. 5. In a semiconductor manufacturing exhaust gas processing equipment equipped with an exhaust device for exhausting exhaust gas from semiconductor manufacturing equipment and an absorbent-filled container filled with a dry absorbent, there is a main air supply between the reaction chamber of the semiconductor manufacturing equipment and the exhaust device. A valve is provided, a bypass pipe having a bypass valve is provided between the inlet side pipe and the outlet side pipe of the absorbent filling container, and an electric circuit for opening and closing the main valve and the bypass valve is provided. Semiconductor manufacturing exhaust gas treatment equipment. 6. The semiconductor manufacturing exhaust gas processing apparatus according to claim 5, wherein the bypass valve is opened by a signal from a pressure detector provided on the inlet side pipe of the absorbent-filled container. 7. The semiconductor manufacturing exhaust gas processing apparatus according to claim 5, wherein the electric circuit includes a timer, and after opening the main valve and the bypass valve, the bypass valve is closed after a predetermined time. 8. The semiconductor manufacturing exhaust gas processing apparatus according to claim 6, wherein the electric circuit is equipped with a timer, and after opening the bypass valve in response to a signal from the pressure sensor, the bypass valve is closed after a predetermined period of time.
JP63238854A 1987-09-25 1988-09-26 Method and apparatus for treating exhaust gas generated from semiconductor production process Granted JPH01281131A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP63238854A JPH01281131A (en) 1987-09-25 1988-09-26 Method and apparatus for treating exhaust gas generated from semiconductor production process

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP62-238859 1987-09-25
JP23885987 1987-09-25
JP63238854A JPH01281131A (en) 1987-09-25 1988-09-26 Method and apparatus for treating exhaust gas generated from semiconductor production process

Publications (2)

Publication Number Publication Date
JPH01281131A true JPH01281131A (en) 1989-11-13
JPH0461686B2 JPH0461686B2 (en) 1992-10-01

Family

ID=26533939

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63238854A Granted JPH01281131A (en) 1987-09-25 1988-09-26 Method and apparatus for treating exhaust gas generated from semiconductor production process

Country Status (1)

Country Link
JP (1) JPH01281131A (en)

Also Published As

Publication number Publication date
JPH0461686B2 (en) 1992-10-01

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