JPH0461686B2 - - Google Patents
Info
- Publication number
- JPH0461686B2 JPH0461686B2 JP63238854A JP23885488A JPH0461686B2 JP H0461686 B2 JPH0461686 B2 JP H0461686B2 JP 63238854 A JP63238854 A JP 63238854A JP 23885488 A JP23885488 A JP 23885488A JP H0461686 B2 JPH0461686 B2 JP H0461686B2
- Authority
- JP
- Japan
- Prior art keywords
- absorbent
- exhaust gas
- semiconductor manufacturing
- bypass valve
- 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 - Lifetime
Links
- 239000007789 gas Substances 0.000 claims description 75
- 239000002250 absorbent Substances 0.000 claims description 53
- 230000002745 absorbent Effects 0.000 claims description 52
- 238000006243 chemical reaction Methods 0.000 claims description 26
- 238000004519 manufacturing process Methods 0.000 claims description 26
- 239000004065 semiconductor Substances 0.000 claims description 26
- 238000000034 method Methods 0.000 claims description 20
- 239000011261 inert gas Substances 0.000 claims description 8
- 238000010926 purge Methods 0.000 claims description 6
- 230000004044 response Effects 0.000 claims description 3
- 238000003672 processing method Methods 0.000 claims 1
- 230000008569 process Effects 0.000 description 9
- 235000012431 wafers Nutrition 0.000 description 7
- 238000005530 etching Methods 0.000 description 5
- 238000009423 ventilation Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000002347 injection Methods 0.000 description 4
- 239000007924 injection Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000006073 displacement reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005268 plasma chemical vapour deposition Methods 0.000 description 2
- 238000001020 plasma etching Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
Landscapes
- Gas Separation By Absorption (AREA)
- Treating Waste Gases (AREA)
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
装置に係り、特に乾式吸収剤によつて処理するの
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 semiconductor manufacturing exhaust gas, and more particularly to a treatment method suitable for treatment with a dry absorbent and its production.
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
り、これにともなつて排ガス処理の必要性が高ま
つてきている。特に最近では、簡便性その他の点
から乾式法により排ガス処理に対する期待が強く
なり、種々のガスに応じた吸収剤が実用に供され
ている。
Dry processes such as plasma CVD and plasma etching are increasingly being adopted in semiconductor manufacturing processes, and with this, the need for exhaust gas treatment is increasing. Particularly in recent years, there have been strong expectations for the dry method for exhaust gas treatment due to its simplicity and other reasons, and absorbents suitable for various gases have been put into practical use.
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、ウエハ処理中に排出さ
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のガスが短時間ではある
が排気されることになる。 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 around several minutes per minute, whereas When evacuation is performed from atmospheric pressure, several thousand gases are exhausted per minute, which corresponds to the rated displacement of the exhaust pump, albeit for a short period of time.
半導体構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、通気抵抗がほとんど表われず、しかも充てん
層内で被処理排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。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
くなり吸収容量の低下を免がれない。そのため多
孔性の吸収剤を使つて吸収容量の向上を計るなど
の試みがなされているが、これらの方法にも限界
があり、結局吸収剤を相当量充てんすることによ
り所定の吸収容量を確保しているのが実状であ
る。また、排ガスによつ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
よつて徐々に充てん層が閉塞されてゆくので通気
抵抗の上昇をまねがれることができない。 When exhaust gas from a semiconductor device 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. In other words, 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 exhaust gas to be treated within the packed layer. . However, in general, coarse absorbents have to be used to keep airflow resistance low; however, as the particle size increases, the surface area involved in absorption or adsorption becomes relatively small, resulting in a decrease in absorption capacity. . For this reason, attempts have been made to improve the absorption capacity by using porous absorbents, but these methods also have limitations, and in the end, it is not possible to secure the specified absorption capacity by filling a considerable amount of absorbent. The reality is that Additionally, some exhaust gases react with absorbents to form solids, and in such cases, even if the absorbent is coarsened, the reaction products will gradually fill the packed layer. Since it becomes blocked, it is impossible to simulate an increase in ventilation resistance.
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つても安全かつ
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.
本発明は半導体製造装置からの排ガスを乾式吸
収剤によつ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
もつ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 using 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. By opening the bypass valve, a large amount of exhaust gas generated when the reaction chamber is evacuated 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 removed. It is characterized in that the gas is replaced with an inert 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エハを処理するもの
であれば形式を問わず、従つてまたプロセスガス
1の種類や流量もそれぞれのプロセスに応じたも
ののいずれであつてもよい。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。 The semiconductor manufacturing equipment 2 can be of any type as long as it processes wafers under high vacuum, such as plasma CVD or plasma etching, and the type and flow rate of the process gas 1 can also be determined according to each process. It's okay. 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.
一般にウエハ処理中には、プロセスガス1は半
導体製造装置の反応室14に導入されてウエハと
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、ウエ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14を大気圧に戻した後に再
度排気装置5によつ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バルブ3が開い
て初めて吐出されるものであるので、バイパス弁
7の開放はメインバルブ3を開放する為の信号に
基いて事前に行なつておけばよい。ただし、メイ
ンバルブ3はエツチング中も開いたままであるの
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の入口圧力が低
くなるのに充分な時間であつて、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 14 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 can be removed by opening the bypass valve 7 and moving the bypass piping 8. The absorbent is discharged without passing through the absorbent filling container 10. At this time, since a large amount of exhaust gas is discharged only after the main valve 3 is opened, the bypass valve 7 may be opened in advance based on a signal for opening the main valve 3. However, since the main valve 3 remains open during etching, the bypass valve 7 also remains open. Therefore, the timer is set to close after a predetermined time, but the timer setting time at that time is sufficient time for the exhaust flow rate to decrease and the inlet pressure of the absorbent filling container 10 to be low, and also for the reaction chamber to be closed. Any time before the process gas is introduced may be used.
また、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が開くと同時に
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うなハンチング現象
が起こる可能性がある。そこでやはりタイマを使
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
閉じるようタイマの時間を設定すれば良い。 In addition, when a large amount of exhaust gas is directly introduced into the absorbent-filled container, the pressure on the inlet side of the container increases, so this pressure increase is detected by the pressure detector 9,
The bypass valve 7 may be opened by the signal.
However, in this case, at the same time as the bypass valve 7 opens, the inlet pressure drops, the pressure detector 9 senses this and closes the bypass valve, and then the pressure rises again and the bypass valve opens, which is a hunting phenomenon. may occur. Therefore, if you use a timer and set the timer to close the bypass valve after exhausting until the inlet pressure is low enough that the bypass valve will not open again even if the exhaust flow rate decreases and the bypass valve is closed. good.
また、ウエ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
されるという事態が生じる。従つて反応室14を
排気する迄に配管に存在している排気ガスを配管
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. It is preferable to release a large amount of 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、また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。さらに注入ガス流量は、パージすべき配管
容積、注入時間等を勘案して決定すれば良い。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 injection period may be either constant injection or only for a certain period of time immediately before exhausting the reaction chamber. good. Further, the flow rate of the injection gas may be determined by taking into account the volume of the piping 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に応用した例を第2図
に基いて説明する。[Embodiment 2] An example in which the present invention is applied to an etching apparatus will be described with reference to FIG.
運転開始前はメインバルブ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
N2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OFFの状態とさ
れ、また、Cl2用弁13−1およびN2用弁13−
2は閉とされ、反応室14は大気圧の状態となつ
ている。 Before the start of operation, the main valve 3 is closed, and the exhaust system 5 is constantly operated, and the exhaust gas is
N2 gas is constantly introduced. Then, the bypass valve 7 is closed, the pressure detection device 9 is turned off, and the Cl 2 valve 13-1 and the N 2 valve 13-
2 is 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内のウエハを設置し蓋を閉め
て密閉すると共にメインバルブ3を開くと反応
室14の大気(20)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/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 operation method of this apparatus will be explained together with its functions: (1) First, a wafer is placed in the reaction chamber 14, and the lid is closed and the main valve 3 is opened. Exhausted by. At this time, since the evacuation speed is high (for example, 1200/min), a large amount of air is introduced into the absorbent-filled 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
〜30/分で設計されているため、排気配管に
初期排気量1200/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 the design flow rate of 0.
~30/min, so when exhaust gas flows into the exhaust piping at an initial displacement rate of 1200/min, the pressure increases.
(2) そこでメインバルブ3が開の信号によつて前
もつてバイパス弁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8を通して排気される。(2) Therefore, by opening the bypass valve 7 in advance in response to a signal indicating that the main valve 3 is open, or by opening the bypass valve 7 by detecting the pressure increase with a pressure detector, it is possible to The portion is mainly exhausted through the bypass pipe 8.
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、Cl2用弁13−1を開として例えば
0.5Sl/分のCl2を反応室14に導入してエツチ
ング反応を行なわせる。(3) Next, open the Cl 2 valve 13-1 and, for example,
0.5 Sl/min of Cl 2 is introduced into the reaction chamber 14 to carry out an etching reaction.
(4) エツチング終了後、Cl2用弁13−1を閉と
し、N2弁用13−2を開として反応室14を
例えば0.5Sl/分のN2ガスにて置換した後N2用
弁13−2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。(4) After etching is completed, close the Cl 2 valve 13-1 and open the N 2 valve 13-2 to replace the reaction chamber 14 with N 2 gas of, for example, 0.5 Sl/min, and then close the N 2 valve. 13-2 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10の容積がある)中は
大気圧であるため大気圧のCl2ガスが残つている
ので、このまゝでは次のバイパスシーケンスには
移ることができない。そこで次のウエハを設置す
る間を利用して導管6より導入される例えば5
/分のN2により該残留Cl2ガスを吸収剤充てん
容器10に導きあらかじめ残留Cl2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
(1)〜(4)の工程をくり返す。 In this state, the pipe from the exhaust device to the adsorbent-filled container (for example, it has a volume of several dozen) is still at atmospheric pressure, so atmospheric pressure Cl 2 gas remains, so if this continues, the next bypass sequence will be carried out. cannot move to. Therefore, for example, 5
By introducing the residual Cl 2 gas into the absorbent-filled container 10 with N 2 /min and evacuating the residual Cl 2 gas in advance, only harmless gas can be bypassed when starting the next operation. Then
Repeat steps (1) to (4).
本発明の処理方法及び装置を半導体製造排ガス
の乾式器処理に用いると、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 dry oven treatment of semiconductor manufacturing exhaust gas, large fluctuations in the flow rate of the exhaust gas can be avoided, and even if an absorbent with a smaller particle size is used, an increase in ventilation resistance can be avoided. This makes it 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。従つて、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 considerably. Even if the reaction efficiency is increased by increasing the surface area, 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り、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
収剤の反応によい固形物が生成する場合であつて
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。 Additionally, because the gas flow rate is low, the contact time with the absorbent is longer, which greatly improves the efficiency of absorbent utilization, and reduces the amount of absorbent required for a given process. The container can also be made compact. Furthermore, even if solids are produced that are good for the reaction between the exhaust gas and the absorbent, the gas flow rate is extremely small, so this does not result in a large ventilation resistance.
また、不活性ガスを使つて常時、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
とにより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 using inert gas to purge the exhaust system and piping system at all times or immediately before exhausting the reaction chamber, not only can the components to be treated be completely delivered to the absorbent-filled container, but also the exhaust system and piping system can be purged using inert gas. can 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
たつて、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 described above, when processing semiconductor manufacturing exhaust gas, a large amount of exhaust gas is discharged when the reaction chamber is evacuated from atmospheric pressure by bypass piping without passing through the absorbent-filled container, and moreover, at that time, there is a large amount of exhaust gas that remains in the piping system. A number of advantages are obtained by previously purging the gas components to be treated with an inert gas up to the absorbent-filled vessel.
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た例を説
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、
3……メインバルブ、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。
FIG. 1 is a diagram schematically showing a flow from a semiconductor manufacturing apparatus to a container filled with an absorbent for exhaust gas, and FIG. 2 is a diagram for explaining an example in which the present invention is applied to an etching apparatus. 1...Process gas, 2...Semiconductor manufacturing equipment,
3... Main valve, 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.
Claims (1)
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項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。[Scope of Claims] 1. When exhausting a 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 downstream of the exhaust system, 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 exhausted. By opening the bypass pipe installed between the inlet side piping and the outlet side piping of the post-absorbent filling chamber, a large amount of exhaust gas is bypassed until the reaction chamber reaches a predetermined pressure, and the absorbent filling chamber and exhaust system are A method for treating semiconductor manufacturing exhaust gas, characterized by avoiding a rise in pressure within the interior. 2. Claim 1, in which the bypass valve is opened based on a signal to open the main valve installed between the reaction chamber and the exhaust device for evacuating the reaction chamber.
A method for treating semiconductor manufacturing exhaust gas as described in . 3. The semiconductor manufacturing exhaust gas recited in claim 1, wherein an increase in inlet pressure is detected by a pressure sensor on the inlet side piping of the absorbent-filled container, and a bypass valve is opened in response to the detected pressure increase signal. Processing method. 4. When evacuating 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 the reaction chamber is evacuated. The semiconductor according to claim 1, 2 or 3, wherein the gas components to be treated are introduced and present in a pipe leading from an exhaust device to an absorbent filling chamber and are detoxified by being sent to an absorbent filling container. How to treat 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 filling container filled with a dry absorbent,
A main valve is provided between the reaction chamber of the semiconductor manufacturing equipment and the exhaust device, a bypass pipe with a bypass valve is provided between the inlet side pipe and the outlet side pipe of the absorbent filling container, and the main valve and an electric circuit for opening and closing a bypass valve. 6. The semiconductor manufacturing exhaust gas processing apparatus according to claim 5, wherein the bypass valve is opened by a signal from a pressure sensor 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 period of 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 detector, the bypass valve is closed after a predetermined period of time.
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 |
|---|---|---|---|
| JP23885987 | 1987-09-25 | ||
| JP62-238859 | 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 JPH01281131A (en) | 1989-11-13 |
| JPH0461686B2 true 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) |
-
1988
- 1988-09-26 JP JP63238854A patent/JPH01281131A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH01281131A (en) | 1989-11-13 |
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