JP2000153128A - Exhaust apparatus - Google Patents

Exhaust apparatus

Info

Publication number
JP2000153128A
JP2000153128A JP10329297A JP32929798A JP2000153128A JP 2000153128 A JP2000153128 A JP 2000153128A JP 10329297 A JP10329297 A JP 10329297A JP 32929798 A JP32929798 A JP 32929798A JP 2000153128 A JP2000153128 A JP 2000153128A
Authority
JP
Japan
Prior art keywords
water
exhaust
vacuum pump
exhaust gas
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.)
Withdrawn
Application number
JP10329297A
Other languages
Japanese (ja)
Inventor
Takayuki Kasukabe
貴之 春日部
Shinji Kikuchi
伸治 菊地
Hiroshi Omatsu
啓 尾松
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.)
Fujitsu Ltd
Shinko Seiki Co Ltd
Original Assignee
Fujitsu Ltd
Shinko Seiki 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 Fujitsu Ltd, Shinko Seiki Co Ltd filed Critical Fujitsu Ltd
Priority to JP10329297A priority Critical patent/JP2000153128A/en
Publication of JP2000153128A publication Critical patent/JP2000153128A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To lower the maintenance cost and operation cost of a vacuum exhaust system and an exhaust gas treatment system and to also enhance safety by enhancing reaction product removing efficiency by enhancing the scrubbing capacity of a water seal type vacuum pump and enhancing the detoxifying efficiency of harmful reaction gas and also reducing the amt. of dilution gas. SOLUTION: An exhaust apparatus is equipped with a gas-water separation tank 11 attached to a water seal type vacuum pump 10 performing the exhaustion of a reactor used in the production of a semiconductor on the exhaust side thereof to introduce the mixed discharged matter of exhaust gas and seal water from the water seal type vacuum pump 10 and forcibly mixing the exhaust gas 12 and seal water in the mixed discharged matter 14 by the exhaust pressure from the water seal type vacuum pump 10 in a contact state to separate and discharge the exhaust gas.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、水封式真空ポンプ
にスクラバ機能をもつ気水分離タンクを組み合わせるこ
とで水封式真空ポンプのスクラバ能力の向上及び反応生
成物除去能率の向上を実現した排気装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention realizes an improvement in the scrubber capacity of a water-sealed vacuum pump and an improvement in the reaction product removal efficiency by combining a water-sealed vacuum pump with a steam-water separation tank having a scrubber function. It relates to an exhaust device.

【0002】[0002]

【従来の技術】一般に、CVD(chemical v
apor deposition)などを実施する減圧
反応装置の排ガス処理を行なう場合、メカニカル・ブー
スタ・ポンプやドライ・ポンプの後段に水封式真空ポン
プを接続して排気システムを構成すると、水封式真空ポ
ンプは減圧反応装置に於ける反応室内の減圧用真空排気
系を構成する最終段真空ポンプとして機能すると共に簡
単で安価、且つ、安全性が高い排ガス除害機能をもつ排
ガス処理系を実現できることが知られている。
2. Description of the Related Art In general, CVD (chemical v)
In the case of performing exhaust gas treatment of a decompression reactor for performing apor deposition, etc., when a water ring vacuum pump is connected to a stage subsequent to a mechanical booster pump or a dry pump to form an exhaust system, the water ring vacuum pump is It is known that it is possible to realize an exhaust gas treatment system having a simple, inexpensive, and highly safe exhaust gas elimination function while functioning as a final-stage vacuum pump constituting a vacuum evacuation system in a reaction chamber in a reduced-pressure reactor. ing.

【0003】この水封式真空ポンプを利用した排ガス処
理系は、減圧反応装置で薄膜を形成する際の排ガス、反
応室内をドライ洗浄した際の排ガスなど、減圧反応装置
に於ける種々な排ガスを処理するのに適用することがで
き、極めて有効な排ガス処理手段であるとされている。
[0003] An exhaust gas treatment system using this water-sealed vacuum pump is capable of removing various exhaust gases in a decompression reactor, such as an exhaust gas when a thin film is formed by a decompression reactor and an exhaust gas when a reaction chamber is dry-cleaned. It is applicable to the treatment and is considered to be an extremely effective exhaust gas treatment means.

【0004】例えば、薄膜を形成する際の排ガス処理に
於いて、SiH4 など、発火性及び爆発性のガスについ
ては、空気などO2 を含むガスを導入してSiO2 とH
2 Oとに変化させ、水封式真空ポンプ内で封水中に取り
込んで安全に処理することができる(要すれば、「特開
昭55−34158号公報」、「特開昭56−1527
号公報」、「特開昭59−197141号公報」などを
参照)。
[0004] For example, in an exhaust gas treatment for forming a thin film, for a flammable or explosive gas such as SiH 4 , a gas containing O 2 such as air is introduced to introduce SiO 2 and H 2.
2 O, and can be taken into sealed water in a water-sealed vacuum pump and safely treated (if necessary, see JP-A-55-34158 and JP-A-56-1527).
No., JP-A-59-197141, etc.).

【0005】また、反応室内をドライ洗浄した際の排ガ
ス処理に於いては、反応室から排出されるクリーニング
・ガス及びガス化した反応生成物を耐蝕性金属で構成さ
れた水封式真空ポンプの封水中に取り込んで除去処理す
ることができる(要すれば、「特開平9−157852
号公報」、を参照)。
In the treatment of exhaust gas when the reaction chamber is dry-cleaned, a cleaning gas discharged from the reaction chamber and a gasified reaction product are supplied to a water ring vacuum pump made of a corrosion resistant metal. It can be taken in sealed water and subjected to removal treatment (if necessary, see Japanese Patent Application Laid-Open No. 9-157852).
Publication).

【0006】その他、Cl2 ,F2 ,HF,HClなど
水と反応するか、或いは、水溶性であるガスを封水中に
取り込むことができる。
In addition, a gas that reacts with water, such as Cl 2 , F 2 , HF, or HCl, or a water-soluble gas can be taken into sealed water.

【0007】このように、水封式真空ポンプは、減圧反
応装置の排ガスに対し、スクラバとして機能させること
ができ、排ガス中の危険且つ有害な未反応ガス、反応ガ
ス、反応生成物などを水と反応させるか、或いは、水に
吸収させるか、或いは、水に溶解させるかなどの種々な
作用に依って、封水中に取り込み処理し、それに続く気
水分離タンクに送り込み、排水と排ガスに分けて排出す
る。
[0007] As described above, the water ring vacuum pump can function as a scrubber for the exhaust gas from the decompression reactor, and removes dangerous and harmful unreacted gas, reaction gas, and reaction products in the exhaust gas. By various actions such as reacting with water or absorbing into water or dissolving in water, taking it into sealed water, treating it into a steam-water separation tank, and separating it into wastewater and exhaust gas. And discharge.

【0008】この水封式真空ポンプがもつスクラバ機能
に依って、減圧反応装置からの排ガスは、乾式除去装置
を介することなく、集合スクラバと結ばれている排気ダ
クトに送り込むことができ、そして、排水は適切な水処
理を経て再利用することができる。
[0008] Due to the scrubber function of the water ring vacuum pump, the exhaust gas from the reduced pressure reactor can be sent to the exhaust duct connected to the collecting scrubber without passing through the dry removal device, and Wastewater can be reused through appropriate water treatment.

【0009】従って、減圧反応装置にとって不可欠であ
る減圧用真空排気系に水封式真空ポンプを用い、それを
利用することに依って、省スペース、安価、安上がりな
保守コストの排ガス処理系を実現することができる。
Therefore, a water-sealed vacuum pump is used for the vacuum evacuation system, which is indispensable for the vacuum reactor, and by using it, an exhaust gas treatment system that is space-saving, inexpensive, and has low maintenance costs is realized. can do.

【0010】ところで、CVDなどを実施する減圧反応
装置からの排ガス中には、前記説明したガスのみでな
く、反応生成物も含まれていることから、真空排気動作
中にポンプ内、或いは、排気管内に粉体化して堆積す
る。
By the way, since the exhaust gas from the decompression reactor for performing CVD or the like contains not only the above-mentioned gas but also a reaction product, the inside of the pump or the exhaust gas is evacuated during the evacuation operation. Powdered and deposited in the tube.

【0011】例えば、CVD法を適用して窒化膜を生成
させるのに用いるNH4 Clなどのガスからは副次的な
反応生成物が発生し、真空排気中に粉体化して硬い膜と
なって被着するので、その除去、洗浄、清掃を行なうこ
とが必須である。
For example, a secondary reaction product is generated from a gas such as NH 4 Cl used to form a nitride film by applying a CVD method, and is powdered during evacuation to form a hard film. Therefore, it is essential to remove, wash and clean it.

【0012】このような反応生成物に対しても水封式真
空ポンプのスクラバ機能は有効に作用し、反応生成物を
封水に溶解して取り込むことができるので、前記したよ
うに減圧用真空排気系の最終段に水封式真空ポンプを設
置して排ガス処理系としても作用させる構成を採ること
に依って、真空排気系内の粉体被着は少なくなって、保
守コストを低く抑えることができる。
[0012] The scrubber function of the water-sealed vacuum pump works effectively on such a reaction product as well, and the reaction product can be dissolved and taken in the sealed water. By installing a water-sealed vacuum pump at the last stage of the exhaust system and acting as an exhaust gas treatment system, powder deposition in the vacuum exhaust system is reduced and maintenance costs are kept low. Can be.

【0013】反応生成物に対して水封式真空ポンプのス
クラバ機能を効果的に発揮させる為には、ポンプや配管
の運転温度を上昇して動作させ、且つ、希釈N2 ガスの
量を調整することに依り、反応生成物をガス状のままで
水封式真空ポンプへと導いて作動封水中に溶解して排水
することが必要である。
In order to effectively exert the scrubber function of the water ring vacuum pump on the reaction product, the operating temperature of the pump and piping is increased and the amount of diluted N 2 gas is adjusted. Therefore, it is necessary to guide the reaction product as it is in a gaseous state to a water-sealed vacuum pump to dissolve it in working sealing water and drain it.

【0014】そのようにすることで、反応生成物はメカ
ニカル・ブースタ・ポンプ、ドライ・ポンプ、配管内に
生成されることはなくなり、また、水封式真空ポンプ内
では作動封水中に溶解するから、結局、真空排気系内、
排ガス処理系内で反応生成物が粉体化、堆積することは
抑止され、保守の周期を延長することができる。
By doing so, the reaction product is not generated in the mechanical booster pump, the dry pump, and the piping, and is dissolved in the working sealing water in the water ring vacuum pump. After all, in the evacuation system,
Pulverization and accumulation of the reaction product in the exhaust gas treatment system are suppressed, and the maintenance cycle can be extended.

【0015】ところで、水封式真空ポンプは、例えばC
VDに於ける未反応ガス及び封水をポンプ本体内で混合
し、その混合物を同一排気口から排出する構成になって
いるので、通常、その排気口は気水分離タンクと呼ばれ
る排水タンクに接続され、そのタンク内で排気ガスと排
水とに分離し、排気ガスは気水分離タンクの排気口か
ら、また、排水は同じく排水口からそれぞれ排出され
る。
Incidentally, a water ring vacuum pump is, for example, C
Since the unreacted gas and sealed water in the VD are mixed in the pump body and the mixture is discharged from the same exhaust port, the exhaust port is usually connected to a drainage tank called a steam separator tank. The exhaust gas is separated into exhaust gas and drainage in the tank, and the exhaust gas is discharged from the exhaust port of the steam separator and the drainage is also discharged from the drain port.

【0016】前記したように、減圧反応装置からの排気
中に含まれる反応生成物は、水封式真空ポンプ内でのス
クラバ機能に依って、作動封水中に溶解されて排出され
るのであるが、その一部は排ガス中に残ってしまい、気
水分離タンクに入ってから排気口から排気ガスとして排
気配管を介し排気ダクトに排出される場合もある。
As described above, the reaction product contained in the exhaust gas from the reduced-pressure reactor is dissolved in the working sealing water and discharged by the scrubber function in the water ring vacuum pump. Some of them may remain in the exhaust gas, and after entering the steam separator, may be discharged from the exhaust port as exhaust gas to the exhaust duct via the exhaust pipe.

【0017】この為、気水分離タンクの排気口や排気配
管内壁で反応生成物が粉体化して堆積し、排気経路を閉
塞する旨の問題が起り、その為の定期的な保守作業が必
要になっている。
[0017] For this reason, the reaction product becomes powdery and accumulates at the exhaust port of the steam separator and the inner wall of the exhaust pipe, causing a problem that the exhaust path is blocked, so that periodic maintenance work is required. It has become.

【0018】[0018]

【発明が解決しようとする課題】本発明では、水封式真
空ポンプのスクラバ能力を向上させて反応生成物の除去
能率を高め、有害な反応ガスの除害能率を高め、希釈ガ
ス量も少なくて済むようにし、真空排気系、排ガス処理
系の保守コスト並びに運転コストを低下させ、且つ、安
全性も向上させる。
SUMMARY OF THE INVENTION In the present invention, the scrubber capacity of a water ring vacuum pump is improved to increase the efficiency of removing reaction products, the efficiency of removing harmful reaction gases, and the amount of diluent gas is reduced. The maintenance cost and operation cost of the vacuum exhaust system and the exhaust gas treatment system are reduced, and the safety is also improved.

【0019】[0019]

【課題を解決するための手段】本発明では、水封式真空
ポンプの排気圧を利用し、排ガスと封水を強制的に混合
接触させ、その接触効率を高めることでスクラバ機能を
向上させることが基本になっている。
SUMMARY OF THE INVENTION In the present invention, the exhaust gas pressure of a water ring vacuum pump is used to forcibly mix and contact exhaust gas and water seal, and the scrubber function is improved by increasing the contact efficiency. Is the basis.

【0020】図1は本発明の原理を説明する為の水封式
真空ポンプを用いたCVD装置用排ガス処理系を表すブ
ロック図である。
FIG. 1 is a block diagram showing an exhaust gas treatment system for a CVD apparatus using a water ring vacuum pump for explaining the principle of the present invention.

【0021】図に於いて、1は反応室、2はSiH4
ス源、3はClF3 ガス源、4並びに5はガス供給管、
6は排ガス排気管、7並びに8はメカニカル・ブースタ
・ポンプ、9はエゼクタ・ポンプ、10は水封式真空ポ
ンプ、11はスクラバ機能をもつ気水分離タンク、12
は吸気ガス、13は作動水、14は吸気ガス12と封水
との混合排出物、15は気水分離タンクからの排ガス、
16はスクラバ機能をもつ気水分離タンクからの排水を
それぞれ示している。
In the figure, 1 is a reaction chamber, 2 is a SiH 4 gas source, 3 is a ClF 3 gas source, 4 and 5 are gas supply pipes,
6 is an exhaust gas exhaust pipe, 7 and 8 are mechanical booster pumps, 9 is an ejector pump, 10 is a water ring vacuum pump, 11 is a steam separation tank having a scrubber function, 12
Is intake gas, 13 is working water, 14 is a mixed discharge of intake gas 12 and sealing water, 15 is exhaust gas from the steam separation tank,
Numeral 16 indicates drainage from the steam separator having a scrubber function.

【0022】前記した吸気ガス12は反応室1からの排
ガスなのであるが、水封式真空ポンプ10が吸引したと
いう意味で特に吸気ガスと呼び、また、作動水13は水
封式真空ポンプ10を通過してから気水分離タンク11
内に在る間は封水と呼ぶことにする。
The above-mentioned intake gas 12 is exhaust gas from the reaction chamber 1 and is particularly called an intake gas in the sense that it is sucked by the water-sealed vacuum pump 10, and the working water 13 is the water-sealed vacuum pump 10. Steam-water separation tank 11 after passing
While inside it will be referred to as sealing.

【0023】図示の排ガス処理系では、水封式真空ポン
プ10が真空排気系の最終段真空ポンプであり、その後
に気水分離タンク11が接続され、その気水分離タンク
11はスクラバ機能をもっていて、吸気ガス12と封水
との混合排出物14が送り込まれた場合、混合排出物1
4が気水分離タンク11内に於いて水封式真空ポンプ1
0からの排気圧に依って強制的に吸気ガス12と封水と
の混合接触が促進されて接触効率が高められる構成にな
っている。
In the illustrated exhaust gas treatment system, a water-sealed vacuum pump 10 is the last-stage vacuum pump of the vacuum evacuation system, and thereafter a steam / water separation tank 11 is connected, and the steam / water separation tank 11 has a scrubber function. When the mixed effluent 14 of the intake gas 12 and the sealing water is sent, the mixed effluent 1
4 is a water-sealed vacuum pump 1 in the steam separation tank 11.
The exhaust gas pressure from 0 forcibly promotes the mixed contact between the intake gas 12 and the sealed water, thereby increasing the contact efficiency.

【0024】実験に依ると、前記スクラバ機能をもつ気
水分離タンク11を取り付けた水封式真空ポンプ10
は、窒化膜を成膜する際の真空排気系及び排ガス処理系
として運転した場合、気水分離タンク11の排気口とダ
クト配管とを結ぶ排気配管内にNH4 Cl生成物粉末が
12箇月で5〔mm〕程度の付着を見たが、これは未だ
正常運転に耐える状態であって洗浄清掃期間は大幅に延
長することが可能である。因みに、スクラバ機能をもた
ない気水分離タンクを用いた場合、前記排気配管内には
NH4 Cl生成物粉末が3箇月で20〔mm〕も付着堆
積する。
According to the experiment, a water ring vacuum pump 10 equipped with the steam-water separation tank 11 having the scrubber function was used.
When operated as a vacuum exhaust system and an exhaust gas treatment system for forming a nitride film, NH 4 Cl product powder is contained in an exhaust pipe connecting an exhaust port of the steam separator 11 and a duct pipe in 12 months. Although adhesion of about 5 [mm] was observed, this is still in a state of withstanding normal operation, and the cleaning and cleaning period can be greatly extended. Incidentally, when a steam-water separation tank having no scrubber function is used, 20 mm of NH 4 Cl product powder adheres and accumulates in the exhaust pipe in three months.

【0025】また、反応室1をドライ洗浄する場合に於
いても、スクラバ機能をもつ気水分離タンク11は有効
であって、従来の気水分離タンクを使用した場合に比較
して排出ガス中のCl2 ,F2 ,HF,HClなどの濃
度が減少し、除害効率の向上が確認された。
Also, in the case where the reaction chamber 1 is dry-cleaned, the steam-water separation tank 11 having a scrubber function is effective. , The concentration of Cl 2 , F 2 , HF, HCl, etc. decreased, and the improvement of the abatement efficiency was confirmed.

【0026】前記したところから、本発明の排気装置に
於いては、半導体製造等に用いる反応装置の排気を行う
水封式真空ポンプ(例えば水封式真空ポンプ10)の排
気側に取り付けられ且つ該水封式真空ポンプからの排ガ
スと封水との混合排出物(例えば混合排出物14)を導
入すると共に該水封式真空ポンプからの排気圧で該混合
排出物中の排ガスと封水とを強制的に混合接触させてか
ら分離して排出する気水分離タンク(例えば気水分離タ
ンク11)を備えてなることを特徴とする。
As described above, in the exhaust device of the present invention, the exhaust device is attached to the exhaust side of a water-sealed vacuum pump (eg, a water-sealed vacuum pump 10) for exhausting a reaction device used for semiconductor manufacturing and the like. A mixed effluent of the exhaust gas from the water-sealed vacuum pump and the sealed water (for example, mixed effluent 14) is introduced, and the exhaust gas and the sealed water in the mixed effluent are discharged by the exhaust pressure of the water-sealed vacuum pump. , And a steam-water separation tank (for example, a steam-water separation tank 11) that separates and discharges after forcibly mixing and contacting.

【0027】前記手段を採ることに依り、排気装置を運
転した場合、水封式真空ポンプのスクラバ能力に気水分
離タンクのスクラバ能力が付加される為、反応生成物の
除去能率は大きく向上し、また、排ガス除害能力も向上
し、従って、希釈ガス量も少なくて済むようになり、真
空排気系、排ガス処理系の保守コスト並びに運転コスト
が低下し、且つ、安全性も向上する。
By employing the above means, when the exhaust system is operated, the scrubber capacity of the water / water separation tank is added to the scrubber capacity of the water ring vacuum pump, so that the efficiency of removing reaction products is greatly improved. In addition, the exhaust gas abatement capacity is improved, so that the amount of diluent gas can be reduced, so that the maintenance cost and operation cost of the vacuum exhaust system and the exhaust gas treatment system are reduced, and safety is improved.

【0028】[0028]

【発明の実施の形態】図2は本発明に於けるスクラバ機
能をもつ気水分離タンクを表す要部切断説明図であり、
図1に於いて用いた記号と同記号は同部分を表すか或い
は同じ意味を持つものとする。尚、図には、水封式真空
ポンプも付記されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 2 is a cutaway view of a main part of a steam / water separation tank having a scrubber function according to the present invention.
The same symbols as those used in FIG. 1 represent the same parts or have the same meaning. It should be noted that the drawing also shows a water ring vacuum pump.

【0029】図に於いて、17はポンプ排気口、21は
混合接触室、22は貯水室、23は分離室、24は排気
管、25は導入管、26はタンクの内壁、27は仕切り
板、29は横断面が矩形をなす樋、36は排水口、38
は排ガス、39はバッフル、40はタンク排気口、42
はドレイン弁、43は連絡管、44は圧力計、45は円
錐底板、46は貯溜封水をそれぞれ示している。
In the drawing, 17 is a pump exhaust port, 21 is a mixing contact chamber, 22 is a water storage chamber, 23 is a separation chamber, 24 is an exhaust pipe, 25 is an inlet pipe, 26 is an inner wall of a tank, and 27 is a partition plate. , 29 are gutters having a rectangular cross section, 36 is a drain port, 38
Is exhaust gas, 39 is a baffle, 40 is a tank exhaust port, 42
Is a drain valve, 43 is a connecting pipe, 44 is a pressure gauge, 45 is a conical bottom plate, and 46 is stored water.

【0030】このスクラバ機能をもつ気水分離タンク1
1は、大別して、中間部に在る混合接触室21、下部に
在る貯水室22、上部に在る分離室23からなってい
て、中間部に在る混合接触室21の中央には、貯水室2
2から分離室23に通じる排気管24が配設され、分離
室23の円錐底板45に達している。
The steam / water separation tank 1 having this scrubber function
1 is roughly divided into a mixing contact chamber 21 in an intermediate part, a water storage chamber 22 in a lower part, and a separation chamber 23 in an upper part. In the center of the mixing contact chamber 21 in the intermediate part, Water storage room 2
An exhaust pipe 24 is provided from 2 to the separation chamber 23, and reaches the conical bottom plate 45 of the separation chamber 23.

【0031】この気水分離タンク11に於いて、水封式
真空ポンプ10が吸引した吸気ガス12及び供給された
作動水13は、水封式真空ポンプ10内で吸気・排気の
動作中に混合されて排気口17から混合排出物14とし
て排出され、導入管25を通じて混合接触室21に送入
される。
In the water / water separation tank 11, the intake gas 12 sucked by the water-sealed vacuum pump 10 and the supplied working water 13 are mixed in the water-sealed vacuum pump 10 during the intake and exhaust operations. Then, the mixture is discharged from the exhaust port 17 as the mixed discharge 14, and is fed into the mixing contact chamber 21 through the introduction pipe 25.

【0032】図3は図2に於いて線X−Xで切断し且つ
矢印方向に見た気水分離タンクの要部切断平面図であ
り、図2に於いて用いた記号と同記号は同部分を表すか
或いは同じ意味を持つものとする。
FIG. 3 is a plan view of an essential part of the water / water separation tank cut along the line XX in FIG. 2 and viewed in the direction of the arrow, and the same symbols as those used in FIG. Parts or have the same meaning.

【0033】図3は導入管25の構成を明らかにするも
のであり、円状をなすタンクの内壁26に沿って接線方
向に設けてあり、水封式真空ポンプ10から排出された
吸気ガス12と封水との混合排出物14はタンクの内壁
26に沿って旋回しながら流下するようになっている。
FIG. 3 clarifies the structure of the inlet pipe 25. The inlet pipe 25 is provided tangentially along the inner wall 26 of the circular tank, and is provided with the intake gas 12 discharged from the water ring vacuum pump 10. The mixed effluent 14 and the sealing water flow down while rotating along the inner wall 26 of the tank.

【0034】図4は気水分離タンクの内部、特に、仕切
り板近傍の構造を明らかにする要部切断側面図であり、
図2及び図3に於いて用いた記号と同記号は同部分を表
すか或いは同じ意味を持つものとする。
FIG. 4 is a cut-away side view of a main part for clarifying the structure inside the steam separator, particularly near the partition plate.
The same symbols as those used in FIGS. 2 and 3 represent the same parts or have the same meaning.

【0035】図に於いて、28は仕切り板27の多孔
部、30は樋29に於ける内側の縁、31は封水、32
は封水31の水膜、33は噴霧、34並びに35は仕切
り板、47は仕切り板34の樋、48は仕切り板35の
樋、49は水面をそれぞれ示している。尚、封水31
は、本来、混合排出物14中の水であるから、排ガスの
一部などが含まれているものである。
In the drawing, 28 is a porous portion of the partition plate 27, 30 is an inner edge of the gutter 29, 31 is water sealing, 32
Denotes a water film of the sealing water 31, 33 denotes a spray, 34 and 35 denote partition plates, 47 denotes a gutter of the partition plate 34, 48 denotes a gutter of the partition plate 35, and 49 denotes a water surface. In addition, sealing water 31
Is originally water in the mixed effluent 14, and contains a part of exhaust gas.

【0036】図から明らかなように、混合接触室21内
の下方には、多数の小孔が設けられた一定幅の多孔部2
8及び樋29からなる仕切り板27、同様な構造の仕切
り板34と35の三層が設けられて貯水室22と仕切ら
れている。尚、仕切り板34のみは、多孔部と大型の樋
47のみで構成されている。
As is apparent from the figure, a porous portion 2 having a fixed width and a large number of small holes is provided below the mixing contact chamber 21.
There are provided a partition plate 27 composed of the pipe 8 and the gutter 29, and three layers of partition plates 34 and 35 having the same structure, and are partitioned from the water storage chamber 22. Note that only the partition plate 34 is composed of only the porous portion and the large gutter 47.

【0037】三層の仕切り板のうち、最上層の仕切り板
27の樋29はタンクの内壁26に沿って全周に設けて
あり、流下した混合排出物14中の水を受けて封水31
として溜めるようになっている。
Out of the three partition plates, the gutter 29 of the uppermost partition plate 27 is provided on the entire circumference along the inner wall 26 of the tank.
It is designed to store as.

【0038】樋29は、適当な幅及び容積をもち、且
つ、水平になっているので、樋29内で満水になった封
水31は内側の縁30を越えて溢出するようになってい
て、また、多孔部28は水量に対して閉口率を調整して
流下量を制限するようになっているので、仕切り板27
上には、一定の厚みの水膜32が形成される。
The gutter 29 has an appropriate width and volume, and is horizontal, so that the sealed water 31 filled with water in the gutter 29 overflows the inner edge 30. Further, since the porous portion 28 is configured to adjust the closing rate with respect to the amount of water to limit the amount of flow, the partition plate 27
A water film 32 having a certain thickness is formed on the upper surface.

【0039】水封式真空ポンプ10は排気圧力をもって
いるので、水膜32にも圧力が加わって、仕切り板27
の多孔部28から封水31の飛沫と排ガスが共に飛散し
て噴霧され、図では、その噴霧を記号33で指示してあ
る。
Since the water ring vacuum pump 10 has an exhaust pressure, the water film 32 is also applied with pressure, and the partition plate 27
The droplets of the sealed water 31 and the exhaust gas are both scattered and sprayed from the porous portion 28, and the spraying is indicated by a symbol 33 in the figure.

【0040】図示されているように、三層の仕切り板2
7,34,35は、それぞれの樋の位置と多孔部の位置
とが入れ替わる構成になっているから、上層の多孔部か
らの噴霧33を下層の樋で受けることになり、樋が満水
になると多孔部に溢出して更に下層の樋へと噴霧される
ことになる。
As shown, the three-layer partition plate 2
7, 34, and 35 are configured such that the position of each gutter and the position of the perforated portion are switched, so that the spray 33 from the upper perforated portion is received by the lower gutter, and when the gutter becomes full. It overflows into the porous part and is sprayed to the lower gutter.

【0041】このように、例えば仕切り板27の多孔部
28に於いて排ガスが水膜32を通過して封水31など
と共に噴霧されて下方の水面49に吹き付ける過程で、
排ガスと封水との接触効率が高まり、排ガスと封水との
反応、吸収、溶解などの作用が効率良く行われ、排ガス
中の危険有害物質は封水中に捕捉されるので、その除
去、除害の効率は向上する。
As described above, for example, in the process in which the exhaust gas passes through the water film 32 and is sprayed together with the sealing water 31 and the like at the porous portion 28 of the partition plate 27 and sprayed onto the lower water surface 49,
The contact efficiency between the exhaust gas and the sealed water increases, and the reaction, absorption, and dissolution of the exhaust gas and the sealed water are performed efficiently.Hazardous substances in the exhaust gas are trapped in the sealed water. The efficiency of harm is improved.

【0042】三層の仕切り板27,34,35を通過し
た封水は貯水室22に溜まって貯溜封水46となり、そ
の貯溜封水46が排水口36の高さを越えると排水16
としてタンク外に排出され、また、封水31の飛沫を含
む排ガス38は貯水室22で流速が低下して、飛沫の分
離落下を行ないつつ移動し、中央の排気管24から上昇
して分離室23へと導かれる。
The sealed water that has passed through the three-layered partition plates 27, 34, and 35 accumulates in the water storage chamber 22 to become the stored sealed water 46. When the stored sealed water 46 exceeds the height of the drain port 36, the drain water 16 is discharged.
The exhaust gas 38 containing the droplets of the sealed water 31 is discharged from the tank at a reduced flow velocity in the water storage chamber 22, moves while separating and dropping the droplets, and rises from the central exhaust pipe 24 to be separated from the separation chamber. It is led to 23.

【0043】分離室23は大きな空間になっているの
で、排ガス38の流速は更に低下して封水飛沫が分離除
去され、排気口40からタンク外へ排気ガス15として
排出される。
Since the separation chamber 23 is a large space, the flow rate of the exhaust gas 38 is further reduced to separate and remove the water-sealed droplets, and the exhaust gas is discharged from the exhaust port 40 to the outside of the tank as the exhaust gas 15.

【0044】バッフル39や分離室23には水滴が凝集
されるが、円錐底板45から排気管24の壁面を伝って
流下して貯水室22に戻る。
Although water droplets are aggregated in the baffle 39 and the separation chamber 23, they flow down from the conical bottom plate 45 along the wall surface of the exhaust pipe 24 and return to the water storage chamber 22.

【0045】混合排出物14中に混在するダストなど固
形粉末は、封水31に溶解することなく分散しているの
であるが、封水31が貯水室22に流下して貯溜封水4
6となって、その一部は排水16と共にタンク外に排出
される。
The solid powder such as dust mixed in the mixed effluent 14 is dispersed without being dissolved in the sealing water 31, but the sealing water 31 flows down to the water storage chamber 22 and the stored sealing water 4.
6 and a part thereof is discharged out of the tank together with the drainage 16.

【0046】然しながら、固形粉末などは貯水室22の
底に堆積することもあるので、その場合にはドレイン弁
42を介して排出すれば良い。
However, since solid powder or the like may accumulate on the bottom of the water storage chamber 22, it may be discharged through the drain valve 42 in such a case.

【0047】混合接触室21と貯水室22とは外部の連
絡管43で結ばれ、その連絡管43内には貯水室22の
貯溜封水46が入り込んでいるので、通常は排ガス38
が流通することはないのであるが、仕切り板27,3
4,35などに於ける多孔部に目詰まりを生ずるなどし
て混合接触室21内の圧力が上昇した場合、連絡管43
介して排ガス38が抜けて安全を維持する。尚、混合接
触室21の圧力上昇は圧力計44で確認することができ
る。
The mixing contact chamber 21 and the water storage chamber 22 are connected by an external communication pipe 43, and the stored sealing water 46 of the water storage chamber 22 enters the communication pipe 43.
Is not distributed, but the partition plates 27, 3
When the pressure in the mixing contact chamber 21 rises due to clogging of the porous portion at 4, 35 or the like, the connecting pipe 43
Exhaust gas 38 escapes via this to maintain safety. The pressure increase in the mixing contact chamber 21 can be confirmed by the pressure gauge 44.

【0048】[0048]

【発明の効果】本発明に依る排気装置に於いては、半導
体製造等に用いる反応装置の排気を行う水封式真空ポン
プの排気側に取り付けられ且つ該水封式真空ポンプから
の排ガスと封水との混合排出物を導入すると共に該水封
式真空ポンプからの排気圧で該混合排出物中の排ガスと
封水とを強制的に混合接触させてから分離して排出する
気水分離タンクを備える。
The exhaust device according to the present invention is mounted on the exhaust side of a water ring vacuum pump for exhausting a reactor used for manufacturing semiconductors and the like, and is sealed with exhaust gas from the water ring vacuum pump. A steam-water separation tank for introducing mixed discharge with water and forcibly mixing and contacting exhaust gas and sealed water in the mixed discharge with exhaust pressure from the water-sealed vacuum pump, and separating and discharging the separated water. Is provided.

【0049】前記構成を採ることに依り、排気装置を運
転した場合、水封式真空ポンプのスクラバ能力に気水分
離タンクのスクラバ能力が付加される為、反応生成物の
除去能率は大きく向上し、また、排ガス除害能力も向上
し、従って、希釈ガス量も少なくて済むようになり、真
空排気系、排ガス処理系の保守コスト及び運転コストを
低下させることができ、且つ、安全性も向上する。
By employing the above configuration, when the exhaust system is operated, the scrubber capacity of the water / water separation tank is added to the scrubber capacity of the water ring vacuum pump, so that the efficiency of removing reaction products is greatly improved. In addition, the exhaust gas abatement capacity is improved, so that the amount of diluent gas can be reduced, so that the maintenance cost and operation cost of the vacuum exhaust system and the exhaust gas processing system can be reduced, and the safety is improved. I do.

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

【図1】本発明の原理を説明する為の水封式真空ポンプ
を用いたCVD装置用排ガス処理系を表すブロック図で
ある。
FIG. 1 is a block diagram showing an exhaust gas treatment system for a CVD apparatus using a water-sealed vacuum pump for explaining the principle of the present invention.

【図2】本発明に於けるスクラバ機能をもつ気水分離タ
ンクを表す要部切断説明図である。
FIG. 2 is a fragmentary explanatory view showing a steam-water separation tank having a scrubber function in the present invention.

【図3】図2に於いて線X−Xで切断し且つ矢印方向に
見た気水分離タンクの要部切断平面図である。
FIG. 3 is a plan view of an essential part of the steam separator, taken along line XX in FIG. 2 and viewed in the direction of the arrow.

【図4】気水分離タンクの内部、特に、仕切り板近傍の
構造を明らかにする要部切断側面図である。
FIG. 4 is a cutaway side view of an essential part for clarifying a structure inside the steam separator, particularly near a partition plate.

【符号の説明】 1 反応室 2 SiH4 ガス源 3 ClF3 ガス源 4並びに5 ガス供給管 6 排ガス排気管 7並びに8 メカニカル・ブースタ・ポンプ 9 エゼクタ・ポンプ 10 水封式真空ポンプ 11 スクラバ機能をもつ気水分離タンク 12 吸気ガス 13 作動水 14 吸気ガス12と封水との混合排出物 15 気水分離タンクからの排ガス 16 スクラバ機能をもつ気水分離タンクからの排水[Description of Signs] 1 Reaction chamber 2 SiH 4 gas source 3 ClF 3 gas source 4 and 5 Gas supply pipe 6 Exhaust gas exhaust pipe 7 and 8 Mechanical booster pump 9 Ejector pump 10 Water ring vacuum pump 11 Scrubber function Steam-water separation tank with 12 Inlet gas 13 Working water 14 Mixture discharge of intake gas 12 and sealing water 15 Exhaust gas from steam-water separation tank 16 Drainage from steam-water separation tank with scrubber function

───────────────────────────────────────────────────── フロントページの続き (72)発明者 菊地 伸治 神奈川県川崎市中原区上小田中4丁目1番 1号 富士通株式会社内 (72)発明者 尾松 啓 滋賀県守山市三宅町30番地 神港精機株式 会社内 Fターム(参考) 3H029 AA07 AA17 AB06 BB34 BB35 BB36 BB37 BB41 BB47 CC22 CC23 CC25 CC42 4D002 AA18 AA19 AA22 AA23 AA26 BA02 BA14 CA03 CA20 DA35 EA05 EA13 GA03 GB04 HA02 ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Shinji Kikuchi 4-1-1, Kamiodanaka, Nakahara-ku, Kawasaki-shi, Kanagawa Prefecture Inside Fujitsu Limited (72) Inventor Kei Omatsu 30 Miyakecho, Moriyama-shi, Shiga Shinko Seiki Intra-company F term (reference) 3H029 AA07 AA17 AB06 BB34 BB35 BB36 BB37 BB41 BB47 CC22 CC23 CC25 CC42 4D002 AA18 AA19 AA22 AA23 AA26 BA02 BA14 CA03 CA20 DA35 EA05 EA13 GA03 GB04 HA02

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】反応装置の排気を行う水封式真空ポンプの
排気側に取り付けられ且つ該水封式真空ポンプからの排
ガスと封水との混合排出物を導入すると共に該水封式真
空ポンプからの排気圧で該混合排出物中の排ガスと封水
とを強制的に混合接触させてから分離して排出する気水
分離タンクを備えてなることを特徴とする排気装置。
1. A water-sealed vacuum pump attached to the exhaust side of a water-sealed vacuum pump for evacuating a reactor, introducing a mixed discharge of exhaust gas and sealed water from the water-sealed vacuum pump and introducing the water-sealed vacuum pump. An exhaust device comprising a steam-water separation tank for forcibly mixing and contacting the exhaust gas and the sealed water in the mixed effluent with the exhaust pressure from the tank and separating and discharging the exhaust gas.
JP10329297A 1998-11-19 1998-11-19 Exhaust apparatus Withdrawn JP2000153128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10329297A JP2000153128A (en) 1998-11-19 1998-11-19 Exhaust apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10329297A JP2000153128A (en) 1998-11-19 1998-11-19 Exhaust apparatus

Publications (1)

Publication Number Publication Date
JP2000153128A true JP2000153128A (en) 2000-06-06

Family

ID=18219897

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10329297A Withdrawn JP2000153128A (en) 1998-11-19 1998-11-19 Exhaust apparatus

Country Status (1)

Country Link
JP (1) JP2000153128A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018523567A (en) * 2015-07-22 2018-08-23 エドワーズ リミテッド Apparatus for exhausting a corrosive effluent gas stream from a processing chamber
JP2019071326A (en) * 2017-10-06 2019-05-09 株式会社ディスコ Brackish water separation tank

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2018523567A (en) * 2015-07-22 2018-08-23 エドワーズ リミテッド Apparatus for exhausting a corrosive effluent gas stream from a processing chamber
JP2019071326A (en) * 2017-10-06 2019-05-09 株式会社ディスコ Brackish water separation tank
JP7132706B2 (en) 2017-10-06 2022-09-07 株式会社ディスコ Steam separation tank

Similar Documents

Publication Publication Date Title
US20110158878A1 (en) Method and device for processing exhaust gas
US10702824B2 (en) Abatement system
AU2008215944B2 (en) Method of treating a gas stream
JP6570794B2 (en) Exhaust gas pressure reduction device
KR20180055343A (en) Gas Scrubber
JP2000279749A (en) Adsorption type gas scrubber for treating gas generated during production of semiconductor
JP3215081B2 (en) Apparatus and method for removing exhaust gas from semiconductor manufacturing
JP2000153128A (en) Exhaust apparatus
JP6874957B2 (en) Exhaust gas abatement emission system
JPH03229609A (en) Dry cvd waste gas treatment device
CN101066521A (en) Exhaust gas treatment
CN1251783C (en) Foam separating and eliminating technology and production line of surface activator
JPS6013071A (en) Evacuating system of device for vapor phase method
KR100503922B1 (en) A separate apparatus for gas and liquid
JP2011143329A (en) Apparatus for detoxifying gas comprising chlorine trifluoride
JP3617575B2 (en) Vacuum exhaust system
KR100790282B1 (en) Ventilation System For Semiconductor Manufacturing Equipment And Liquid TEOS Exhausting Method In Trap Employed Therein
JP3433998B2 (en) Filtration apparatus and vacuum pump system protection method using the same
JPH05212232A (en) Dry collecting method of solid particles from solid particle-containing gas fluid
KR20150094534A (en) Exhausting line for manufacturing system with sub-vaccum means
KR20020033941A (en) Waste gas treatment system
KR20030052170A (en) Powder trap device of a semiconductor manufacture equipment
KR20030022532A (en) complex filtering system of gas
JPH01123616A (en) Washing tower
JP2005264851A (en) Trap device and its regenerating method

Legal Events

Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 20060207