JP2003024741A - Combustion type semiconductor exhaust gas treatment apparatus - Google Patents

Combustion type semiconductor exhaust gas treatment apparatus

Info

Publication number
JP2003024741A
JP2003024741A JP2001216742A JP2001216742A JP2003024741A JP 2003024741 A JP2003024741 A JP 2003024741A JP 2001216742 A JP2001216742 A JP 2001216742A JP 2001216742 A JP2001216742 A JP 2001216742A JP 2003024741 A JP2003024741 A JP 2003024741A
Authority
JP
Japan
Prior art keywords
exhaust gas
type semiconductor
combustion
combustion type
semiconductor 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.)
Pending
Application number
JP2001216742A
Other languages
Japanese (ja)
Inventor
Shinichiro Nomura
伸一郎 野村
Yasutsune Katsuta
康常 勝田
Akira Baba
彰 馬場
Fumihiko Hanayama
文彦 花山
Noboru Takarayama
登 寳山
Kenji Kumagai
健志 熊谷
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP2001216742A priority Critical patent/JP2003024741A/en
Publication of JP2003024741A publication Critical patent/JP2003024741A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

Abstract

PROBLEM TO BE SOLVED: To provide a combustion type semiconductor exhaust gas treatment apparatus preventing the adhesion of a silica powder, which is a combustion decomposed product of a monosilane contained in the exhaust gas of a semiconductor manufactur process, to piping during a feed process. SOLUTION: In the combustion type semiconductor exhaust gas treatment apparatus having a combustion furnace 3 of gas to be treated, a cooling part 4 provided under the combustion furnace, a tank 6 provided under the cooling part to receive cooling water and an absorption column 7 provided to the cooling part on the downstream side thereof, the tank 6 provided under the cooling part is extended to the region under the absorption column 7 and a space part 6A is provided between the cooling part 4 and the lower part of the absorption column 7 so as to introduce the gas discharged from the cooling part 4 into the lower part of the absorption column 7.

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】本発明は燃焼式半導体排ガス
処理装置に関し、さらに詳しくは、半導体製造プロセス
から排出されるモノシランおよびフロンガスを効率よく
除去することのできる燃焼式半導体排ガス処理装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combustion type semiconductor exhaust gas treatment device, and more particularly to a combustion type semiconductor exhaust gas treatment device capable of efficiently removing monosilane and freon gas discharged from a semiconductor manufacturing process.

【0002】[0002]

【従来の技術】近年地球温暖化の問題がクローズアップ
されており、化石燃料を大量に消費して生成される一酸
化炭素、二酸化炭素等の排ガスの排出量を抑制すること
が求められている。半導体製造プロセスから排出される
フロンガス(PFC: パーフルオロカーボン)は総排
出量は少ないが、地球温暖化係数は二酸化炭素CO2
1000倍から10000倍といわれており、半導体生
産が今後も増加することを考慮すると無視できない。気
候変動枠組み条約締約国会議の京都議定書(1997
年)においても、PFCは削減対象の温室効果ガスの一
つに挙げられている。このような状況に鑑み、フロンを
無害化する排ガス処理装置の開発が必要とされている。
2. Description of the Related Art In recent years, the problem of global warming has been highlighted, and it is required to suppress the emission of exhaust gas such as carbon monoxide and carbon dioxide produced by consuming a large amount of fossil fuel. . The total amount of CFCs emitted from semiconductor manufacturing processes (PFC: Perfluorocarbon) is small, but the global warming potential is said to be 1,000 to 10,000 times that of carbon dioxide CO 2 , and semiconductor production will continue to increase. Can not be ignored considering. Kyoto Protocol (1997) of the Conference of the Parties to the Framework Convention on Climate Change
(Year), PFC is listed as one of the greenhouse gases to be reduced. In view of such a situation, it is necessary to develop an exhaust gas treatment device that makes CFCs harmless.

【0003】排ガス処理装置の方式には、湿式、触媒式
等があるが、これらはランニングコストが高い等の問題
があり、装置自体が比較的コンパクトでランニングコス
トの低い燃焼式による処理装置の開発が期待されてい
る。半導体製造プロセスの排ガスにはフロンの他にもモ
ノシランなどの有害な成分があり、燃焼炉内ではフロン
を分解するとともにこれら有害ガスも分解しなければな
らず、燃焼分解後のガス中にはフロンガス分解で生成す
るフッ化水素の他にモノシランガス分解で生成するシリ
カ粉が存在することとなる。
There are various types of exhaust gas treatment apparatus, such as a wet type and a catalytic type, but these have problems such as high running cost, and the development of a combustion type processing apparatus having a relatively compact apparatus and low running cost. Is expected. Exhaust gas from the semiconductor manufacturing process contains harmful components such as monosilane in addition to CFCs. In the combustion furnace, CFCs must be decomposed and these harmful gases must also be decomposed. In addition to hydrogen fluoride generated by decomposition, silica powder generated by decomposition of monosilane gas is present.

【0004】図2は、従来の代表的な燃焼式半導体排ガ
ス処理装置の概略構造を示す説明図である。被処理ガス
21は排ガス入口から燃焼炉22に導入され、燃焼分解
する。燃焼炉22の下方には燃焼ガスを冷却する冷却部
23が設けられており、そこでモノシランの分解で生成
したシリカ粉およびフロンガス分解で生成したフッ化水
素の部分的な捕集除去が行なわれる。冷却部23の下方
にはシリカ粉の捕集を行なうためのサイクロンスクレー
パ方式の集塵装置24が設けられ、ここでシリカ粉が除
去された後、排ガスは吸収塔25に供給され、吸収塔2
5で排ガスからフッ化水素が完全除去された後、有害成
分を含まない処理ガス27は、吸収塔上部から外部に排
出される。フッ化水素を吸収した酸排水26は一旦吸収
塔下部のタンクに貯留された後、外部に排出される。
FIG. 2 is an explanatory view showing the schematic structure of a conventional typical combustion type semiconductor exhaust gas treating apparatus. The to-be-processed gas 21 is introduced into the combustion furnace 22 through the exhaust gas inlet and decomposed by combustion. A cooling unit 23 that cools the combustion gas is provided below the combustion furnace 22, and the silica powder generated by the decomposition of monosilane and the hydrogen fluoride generated by the decomposition of Freon gas are partially collected and removed. Below the cooling unit 23, a cyclone scraper type dust collector 24 for collecting silica powder is provided. After the silica powder is removed here, the exhaust gas is supplied to the absorption tower 25 and the absorption tower 2
After the hydrogen fluoride is completely removed from the exhaust gas in 5, the processing gas 27 containing no harmful component is discharged to the outside from the upper part of the absorption tower. The acid wastewater 26 that has absorbed hydrogen fluoride is temporarily stored in a tank below the absorption tower and then discharged to the outside.

【0005】図3は、従来の他の燃焼式半導体排ガス処
理装置の概略構造を示す説明図である。被処理ガスは排
ガス入口30から燃焼炉31に導入され、燃焼分解す
る。燃焼炉31の下方には燃焼ガスを冷却する冷却部3
2が設けられ、さらに冷却部32と連通する管路端には
冷却部33が設けられ、それぞれモノシランの分解で生
成したシリカ粉およびフロンガス分解で生成したフッ化
水素の部分的な捕集除去が行なわれる。冷却部33と連
通する管路端にはさらにスクラバ装置36が設けられ、
ここでシリカ粉の捕集とフッ化水素の湿式除去が行なわ
れる。該スクラバ装置を出た排ガスはミストトラップ3
7を通して、ミストが除去された後、処理ガス出口39
から排気される。
FIG. 3 is an explanatory view showing the schematic structure of another conventional combustion type semiconductor exhaust gas treating apparatus. The gas to be treated is introduced into the combustion furnace 31 through the exhaust gas inlet 30 and decomposed by combustion. Below the combustion furnace 31, there is a cooling unit 3 for cooling the combustion gas.
2 is provided, and further, a cooling unit 33 is provided at the end of the conduit communicating with the cooling unit 32, so as to partially collect and remove silica powder produced by decomposition of monosilane and hydrogen fluoride produced by decomposition of Freon gas. Done. A scrubber device 36 is further provided at the end of the pipeline communicating with the cooling unit 33,
Here, the collection of silica powder and the wet removal of hydrogen fluoride are performed. The exhaust gas leaving the scrubber device is a mist trap 3.
After the mist is removed through 7, the process gas outlet 39
Exhausted from.

【0006】これら従来の燃焼式半導体排ガス処理装置
では、モノシランの燃焼分解で生成したシリカ粉は、燃
焼ガスとともに、燃焼炉から冷却部、さらにその後流側
にある、集塵部、吸収塔へと搬送される。しかし、これ
ら従来の装置では、被処理ガス搬送の過程でシリカ粉が
途中の配管内に付着し、それにより配管が閉塞してしま
い、そのために装置の連続運転が妨げられ、結局モノシ
ランやフロンガスの効率的な除去が図れない、という諸
々の問題点があった。
In these conventional combustion type semiconductor exhaust gas treatment apparatuses, silica powder produced by the combustion decomposition of monosilane flows from the combustion furnace to the cooling section and further to the dust collecting section and the absorption tower on the downstream side together with the combustion gas. Be transported. However, in these conventional devices, silica powder adheres to the inside of the pipe in the process of transporting the gas to be treated, which clogs the pipe, which hinders continuous operation of the device, and eventually results in monosilane or fluorocarbon gas. There were various problems that efficient removal could not be achieved.

【0007】[0007]

【発明が解決しようとする課題】本発明の課題は、上記
従来技術の欠点を除き、半導体製造プロセスの排ガスに
含まれるモノシランの燃焼分解生成物であるシリカ粉
が、搬送過程中に配管に付着することを防止して、配管
の閉塞の問題を起こさず、これにより連続運転が可能な
燃焼式半導体排ガス処理装置を提供することである。
The object of the present invention is to eliminate the drawbacks of the prior art described above, and silica powder, which is a combustion decomposition product of monosilane contained in the exhaust gas of the semiconductor manufacturing process, adheres to the pipe during the transportation process. The present invention is to provide a combustion type semiconductor exhaust gas treatment device which prevents continuous operation and thus does not cause a problem of pipe clogging, thereby enabling continuous operation.

【0008】[0008]

【課題を解決するための手段】上記課題を達成するた
め、本願で特許請求される発明は以下のとおりである。 (1)被処理ガスを燃焼分解するための燃焼炉と、該燃
焼炉の下方に設けられた、燃焼後の被処理ガスを水冷却
するための冷却部と、該冷却部の下方に設けられた、冷
却水を受け入れるためのタンクと、該冷却部の後流側に
設けられた、該ガス中のフッ化水素を吸着するための湿
式吸収塔とを有する燃焼式半導体排ガス処理装置におい
て、前記冷却部の下方に設けたタンクを前記吸収塔下方
まで延設し、前記冷却部と前記吸収塔下部との間に、該
冷却部から排出されたガスが該吸収塔下部に導入される
ように空間部を設けたことを特徴とする燃焼式半導体排
ガス処理装置。
In order to achieve the above object, the invention claimed in the present application is as follows. (1) A combustion furnace for combusting and decomposing a gas to be treated, a cooling unit provided below the combustion furnace for cooling the gas to be treated after burning with water, and a cooling unit provided below the cooling unit. A combustion type semiconductor exhaust gas treatment apparatus having a tank for receiving cooling water and a wet absorption tower for adsorbing hydrogen fluoride in the gas, which is provided on the downstream side of the cooling unit, wherein: A tank provided below the cooling unit is extended to below the absorption tower, and the gas discharged from the cooling unit is introduced into the lower part of the absorption tower between the cooling unit and the lower part of the absorption tower. A combustion type semiconductor exhaust gas treatment device, characterized by having a space portion.

【0009】(2)前記被処理ガスがモノシランを含む
ものである、(1)記載の燃焼式半導体排ガス処理装
置。 (3)前記吸収塔の後流側に、シリカ粉を捕集するため
の、バグフィルタ式集塵装置を設けた、(1)または
(2)記載の燃焼式半導体排ガス処理装置。 (4)前記燃焼式半導体排ガス処理装置において、前記
空間部を保持するために、該タンク内の水面レベルの上
限を所定値以下に制御する手段を設けた、(1)ないし
(3)記載の燃焼式半導体排ガス処理装置。
(2) The combustion type semiconductor exhaust gas treating apparatus according to (1), wherein the gas to be treated contains monosilane. (3) The combustion type semiconductor exhaust gas treatment device according to (1) or (2), wherein a bag filter type dust collecting device for collecting silica powder is provided on the downstream side of the absorption tower. (4) In the combustion type semiconductor exhaust gas treating apparatus, in order to hold the space, means for controlling the upper limit of the water surface level in the tank to a predetermined value or less is provided, (1) to (3) Combustion type semiconductor exhaust gas treatment equipment.

【0010】(5)前記燃焼式半導体排ガス処理装置に
おいて、該燃焼炉の側壁(外周壁と称す)の内側に高温
耐熱性多孔物質で構成されたもう一つの側壁(内周壁と
称す)を設け、該内周壁を通して気体が燃焼炉内部に送
入されるようにしたことを特徴とする、(1)記載の燃
焼式半導体排ガス処理装置。 (6)前記燃焼式半導体排ガス処理装置において、燃焼
炉の外周壁と内周壁との空間が分割されていて、それぞ
れの空間へ気体送入手段を設けられていることを特徴と
する、(5)記載の燃焼式半導体排ガス処理装置。 (7)前記燃焼式半導体排ガス処理装置において、内周
壁を通して燃焼炉内部に送入する気体が空気または窒素
であることを特徴とする、(6)記載の燃焼式排ガス処
理装置。
(5) In the above combustion type semiconductor exhaust gas treating apparatus, another side wall (referred to as inner peripheral wall) made of a high temperature heat resistant porous material is provided inside the side wall (referred to as outer peripheral wall) of the combustion furnace. The gas is introduced into the combustion furnace through the inner peripheral wall of the combustion type semiconductor exhaust gas treatment apparatus according to (1). (6) In the combustion type semiconductor exhaust gas treating apparatus, the space between the outer peripheral wall and the inner peripheral wall of the combustion furnace is divided, and a gas feeding means is provided in each space. ) Combustion type semiconductor exhaust gas treatment device as described above. (7) In the combustion-type semiconductor exhaust gas treatment device, the gas introduced into the combustion furnace through the inner peripheral wall is air or nitrogen, (6).

【0011】本発明は、燃焼式半導体排ガス処理装置に
おいて、燃焼炉の下方に設けられた水スプレによる冷却
部の下方に冷却水を受け入れるタンクを設置し、これを
湿式吸収塔下方にまで延設し、冷却部から排出されたガ
スが吸収塔下部に導入されるように空間部を設けたこと
により、燃焼後被処理ガス搬送用の配管を構造上省略
し、シリカ粉の付着を防止することができる。また本発
明装置では、冷却部から排出された燃焼後の被処理ガス
は、タンク内天井面とタンク内に溜まっている水の表面
との間の空間部を通して、吸収塔下部へと導入される。
該空間部はガスの搬送に充分な容積を有し、また該空間
部の重力方向底面は水面であるためシリカ粉の付着は発
生しない。さらに、シリカ粉のタンク天井表面への一時
的付着が発生しても、付着したシリカ粉は自重で下方水
面上に落下するため、タンク内空間部のシリカ粉の付着
による閉塞は、完全に防止することができる。
According to the present invention, in a combustion type semiconductor exhaust gas treating apparatus, a tank for receiving cooling water is installed below a cooling section by a water spray provided below a combustion furnace, and the tank is extended below a wet absorption tower. However, by providing a space part so that the gas discharged from the cooling part is introduced into the lower part of the absorption tower, the piping for conveying the gas to be treated after combustion is structurally omitted, and the adhesion of silica powder is prevented. You can Further, in the device of the present invention, the post-combustion target gas discharged from the cooling section is introduced to the lower part of the absorption tower through the space between the ceiling surface of the tank and the surface of the water accumulated in the tank. .
Since the space has a sufficient volume for transporting gas, and the bottom surface of the space in the gravity direction is the water surface, adhesion of silica powder does not occur. Further, even if the silica powder temporarily adheres to the surface of the tank, the silica powder that adheres falls to the lower water surface by its own weight, so clogging due to the adhesion of silica powder in the space inside the tank is completely prevented. can do.

【0012】[0012]

【発明の実施の形態】以下、本発明を図面に示す実施例
により、さらに詳細に説明する。図1は、本発明の燃焼
式半導体排ガス処理装置の概略構造を示す説明図であ
る。図において、本装置は、被処理ガスを燃焼分解する
ための燃焼炉3と、該燃焼炉の下方に設けられた、燃焼
後の被処理ガスを水冷却するための冷却部4と、前記冷
却部4の下方に設けられ、かつ吸収塔7の下方まで延設
された、前記冷却部4からの水または該吸収塔7からの
洗浄水の少なくともいずれかを受けるためのタンク6
と、前記冷却部4の後流側で、かつ前記延設されたタン
ク6の上方に設けられた、ガス中のフッ化水素を吸着す
るための湿式吸収塔7とから主として構成される。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will now be described in more detail with reference to the embodiments shown in the drawings. FIG. 1 is an explanatory view showing a schematic structure of a combustion type semiconductor exhaust gas treatment apparatus of the present invention. In the figure, the present apparatus comprises a combustion furnace 3 for burning and decomposing a gas to be treated, a cooling unit 4 provided below the combustion furnace for water-cooling the gas to be treated after combustion, and the cooling unit. A tank 6 provided below the section 4 and extending below the absorption tower 7 for receiving at least either water from the cooling section 4 or washing water from the absorption tower 7.
And a wet absorption tower 7 for adsorbing hydrogen fluoride in the gas, which is provided on the downstream side of the cooling unit 4 and above the extended tank 6.

【0013】前記冷却部4と前記吸収塔7下部との間に
設けられた前記タンク6の内部には、該冷却部4から排
出されたガスが該吸収塔7下部に導入されるようにする
ための空間部6Aが形成されている。該空間部6Aは該
ガスの搬送に充分な容積を有するように形成されてい
る。さらに上記タンク6には、該タンク6内の水面レベ
ルを監視するためのレベル計11、および該タンク6底
部から水を排出するための排水ポンプ12が設けられて
いる。
The gas discharged from the cooling unit 4 is introduced into the lower portion of the absorption tower 7 inside the tank 6 provided between the cooling unit 4 and the lower portion of the absorption tower 7. A space portion 6A for forming the space is formed. The space 6A is formed to have a sufficient volume for carrying the gas. Further, the tank 6 is provided with a level gauge 11 for monitoring the water surface level in the tank 6 and a drainage pump 12 for discharging water from the bottom of the tank 6.

【0014】図1において、被処理ガスであるモノシラ
ンやフロンガスを含む半導体排ガスは、処理ガス導入管
1から燃焼炉3上部に導入され、該燃焼炉3上部に設け
られたバーナ2により着火され、該燃焼炉3内にて燃焼
分解される。被処理ガス中のモノシランが前記燃焼炉3
で燃焼されることにより、分解生成物であるシリカがシ
リカ粉として生成する。シリカ粉を含む、高温の燃焼後
の処理ガスは、前記燃焼炉3下方に設けられた冷却部4
に導入され、スプレノズル5から噴出されるスプレ水に
より冷却される。該ガスの冷却に用いられたスプレ水
は、前記冷却部4の下方に設けられ、かつ吸収塔7の下
方まで延設されたタンク6に落下し溜められる。該タン
ク6内部には、該スプレ水の他、後述する吸収塔7から
落下する洗浄水も受水して溜められる。これらの水の貯
留により該タンク6内部上方には、該タンク6内壁表面
および貯留水の水面により空間部6Aが形成され、該冷
却部4から排出されたガスは該空間部6Aを通して前記
吸収塔7下部に導入される。
In FIG. 1, a semiconductor exhaust gas containing monosilane or chlorofluorocarbon as a gas to be treated is introduced from a treatment gas introducing pipe 1 into an upper part of a combustion furnace 3 and ignited by a burner 2 provided in an upper part of the combustion furnace 3. Combustion is decomposed in the combustion furnace 3. The monosilane contained in the gas to be treated is the combustion furnace 3
By being combusted with, the decomposition product silica is generated as silica powder. The high-temperature post-combustion process gas containing silica powder is cooled by a cooling unit 4 provided below the combustion furnace 3.
And is cooled by the spray water which is introduced into the spray nozzle 5 and is sprayed from the spray nozzle 5. The spray water used for cooling the gas is dropped and stored in a tank 6 provided below the cooling unit 4 and extending below the absorption tower 7. Inside the tank 6, in addition to the spray water, washing water falling from an absorption tower 7 described later is received and stored. By storing these water, a space 6A is formed above the inside of the tank 6 by the inner wall surface of the tank 6 and the surface of the stored water, and the gas discharged from the cooling unit 4 passes through the space 6A to the absorption tower. 7 is introduced at the bottom.

【0015】該吸収塔7内に導入された該ガスは、充填
層10に導入される。該充填層10には、該充填層10
の上方に設けられたスプレノズル9からスプレ水が噴出
され、該充填層10内に導入された該ガスは、該スプレ
水と接触し、これにより該ガス中のフロンガス燃焼分解
生成物であるフッ化水素は該スプレ水に吸収され、該ガ
ス中から除去される。フッ化水素を吸収した該スプレ水
は、洗浄水として前記吸収塔9内を落下し、該吸収塔9
下方に延設されている前記タンク6に受け入れられ、溜
められる。上記タンク6内の貯留水面レベルはレベル計
11により監視され、水面レベルが一定の上限を超えな
いよう、排水ポンプ12により排出する水量が調整され
る。
The gas introduced into the absorption tower 7 is introduced into the packed bed 10. The packed bed 10 includes the packed bed 10
Spray water is jetted from a spray nozzle 9 provided above the gas, and the gas introduced into the packed bed 10 comes into contact with the spray water, whereby fluorinated gas which is a CFC gas combustion decomposition product in the gas. Hydrogen is absorbed by the spray water and removed from the gas. The spray water that has absorbed hydrogen fluoride falls in the absorption tower 9 as washing water,
It is received and stored in the tank 6 extending downward. The level of water stored in the tank 6 is monitored by the level meter 11, and the amount of water discharged by the drainage pump 12 is adjusted so that the water level does not exceed a certain upper limit.

【0016】前記タンク6内壁表面および貯留水の水面
により形成された、空間部6Aの重力方向底面は水面で
あるため、前記冷却部4から排出され該空間部6Aを通
して前記吸収塔9下部へと導入される燃焼後の被処理ガ
ス中のモノシラン燃焼分解生成物であるシリカ粉の、該
空間部6Aへの付着は発生しない。また該空間部6Aは
該ガスの搬送に充分な容積を有するため、該ガスの該吸
収塔9下部への導入は、充分に行われる。さらに、シリ
カ粉の該タンク6天井表面への一時的付着が発生して
も、付着したシリカ粉は自重で下方の貯留水面上に落下
するため、該空間部6Aのシリカ粉の付着による閉塞
は、完全に防止することができる。
Since the bottom surface of the space 6A formed by the inner wall surface of the tank 6 and the water surface of the stored water in the direction of gravity is the water surface, the space 6A is discharged from the cooling section 4 to the lower part of the absorption tower 9 through the space 6A. The silica powder, which is a combustion decomposition product of monosilane in the introduced gas to be treated after combustion, does not adhere to the space 6A. Further, since the space 6A has a sufficient volume for transporting the gas, the gas is sufficiently introduced into the lower part of the absorption tower 9. Furthermore, even if the silica powder temporarily adheres to the ceiling surface of the tank 6, the silica powder that adheres falls on the stored water surface below due to its own weight, so that the space 6A is not clogged due to the adhesion of the silica powder. , Can be completely prevented.

【0017】吸収塔7の後流側にバグフィルタのような
シリカ粉集塵装置8が設けられ、該バグフィルタは吸引
ファン(IDF)13により吸引されて、該ガス中に含
まれる未捕集のシリカ粉が捕集され、該ガスはシリカ粉
が除去された後、装置外へ排出される。図1におけるバ
ーナ2は、被処理ガスが該バーナ2本体の外部から導入
され、燃焼用空気と燃料が該バーナ2内部で予混合され
るような構造のものを示したが、本発明においては、例
えば被処理ガスが該バーナ2内部から導入され、燃焼用
空気と燃料が該バーナ2本体の外部から送入されるよう
な構造のものでもよい。
A silica powder dust collector 8 such as a bag filter is provided on the downstream side of the absorption tower 7. The bag filter is sucked by a suction fan (IDF) 13 and is not trapped in the gas. Of the silica powder is collected, and the gas is discharged to the outside of the apparatus after the silica powder is removed. The burner 2 in FIG. 1 has a structure in which the gas to be treated is introduced from the outside of the main body of the burner 2 and combustion air and fuel are premixed inside the burner 2, but in the present invention, For example, the gas to be treated may be introduced from the inside of the burner 2, and the combustion air and the fuel may be introduced from the outside of the main body of the burner 2.

【0018】図1における燃焼炉3は、燃料が該燃焼炉
3の上方から送入されるものを示したが、該燃焼炉3の
壁(外周壁と称す)の内側に、もう一つの側壁(内周壁
と称す)を設け、内周壁を通して気体が燃焼炉内部に送
入される構造のものでもよい。図4では縦方向仕切り板
58と横方向仕切り板59によって8分割しているもの
を示している。図示していないが、それぞれの分割空間
には気体送入ラインが接続されている。このような形状
の燃焼炉とすると、生成したシリカが炉壁に付着するの
を防止でき、生成したシリカをタンク6へ落とし込める
ので、装置全体としてつまりを発生しないものとなる。
In the combustion furnace 3 in FIG. 1, fuel is fed from above the combustion furnace 3, but inside the wall of the combustion furnace 3 (referred to as an outer peripheral wall), another side wall is provided. (Inner peripheral wall) may be provided, and gas may be introduced into the combustion furnace through the inner peripheral wall. In FIG. 4, the vertical partition plate 58 and the horizontal partition plate 59 are shown as being divided into eight parts. Although not shown, a gas inlet line is connected to each divided space. With the combustion furnace having such a shape, the generated silica can be prevented from adhering to the furnace wall, and the generated silica can be dropped into the tank 6, so that the device as a whole does not generate clogging.

【0019】[0019]

【発明の効果】請求項1ないし4記載の発明によれば、
燃焼式半導体排ガス処理装置において、半導体製造プロ
セスの排ガスに含まれるシリカ粉等が搬送過程中に配管
に付着することを防止して、配管の閉塞の問題を起こさ
ないため、装置の連続運転が可能となり、長時間にわた
る安定燃焼を確保することができ、また、燃焼炉から冷
却部および吸収塔への配管を省略した低ユーティリティ
ーの構造とすることができる。さらに、シリカ粉による
配管等の閉塞がないため、シリカ粉の捕集効率をほぼ1
00%とすることができる。
According to the inventions of claims 1 to 4,
In a combustion type semiconductor exhaust gas treatment device, silica powder contained in the exhaust gas of the semiconductor manufacturing process is prevented from adhering to the pipe during the transportation process, and the problem of pipe clogging does not occur, so continuous operation of the device is possible As a result, stable combustion can be secured for a long time, and a low utility structure in which pipes from the combustion furnace to the cooling unit and the absorption tower are omitted can be obtained. Furthermore, since there is no clogging of the piping etc. by silica powder, the collection efficiency of silica powder is almost 1
It can be set to 00%.

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

【図1】本発明の燃焼式半導体排ガス処理装置の概略構
造を示す説明図。
FIG. 1 is an explanatory diagram showing a schematic structure of a combustion type semiconductor exhaust gas treatment apparatus of the present invention.

【図2】従来の代表的な燃焼式半導体排ガス処理装置の
概略構造を示す説明図。
FIG. 2 is an explanatory diagram showing a schematic structure of a conventional typical combustion type semiconductor exhaust gas treatment apparatus.

【図3】従来の代表的な燃焼式半導体排ガス処理装置の
概略構造を示す説明図。
FIG. 3 is an explanatory view showing a schematic structure of a conventional typical combustion type semiconductor exhaust gas treatment apparatus.

【図4】本発明の燃焼炉の構造を示す説明図。FIG. 4 is an explanatory view showing the structure of a combustion furnace of the present invention.

【符号の説明】[Explanation of symbols]

1…処理ガス導入管、2…バーナ、3…燃焼炉、4…冷
却部、5…スプレノズル、6…タンク、6A…空間部、
7…吸収塔、8…集塵装置、9…吸収塔スプレノズル、
10…充填層、11…レベル計、12…排水ポンプ、1
3…吸引ファン(IDF)。
1 ... Process gas introduction pipe, 2 ... Burner, 3 ... Combustion furnace, 4 ... Cooling part, 5 ... Spray nozzle, 6 ... Tank, 6A ... Space part,
7 ... Absorption tower, 8 ... Dust collector, 9 ... Absorption tower spray nozzle,
10 ... Packed bed, 11 ... Level meter, 12 ... Drainage pump, 1
3 ... Suction fan (IDF).

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) // H01L 21/205 F23J 15/00 J (72)発明者 馬場 彰 広島県呉市宝町3番36号 バブコック日立 株式会社呉研究所内 (72)発明者 花山 文彦 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 (72)発明者 寳山 登 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 (72)発明者 熊谷 健志 広島県呉市宝町6番9号 バブコック日立 株式会社呉事業所内 Fターム(参考) 3K070 DA05 DA24 DA27 DA28 DA37 3K078 AA06 BA20 BA29 CA03 CA12 4D002 AA23 AA26 AC10 BA02 BA05 BA13 BA14 CA01 CA07 CA13 CA20 DA35 EA02 FA10 HA03 4K030 AA06 CA04 CA12 EA12 KA26 5F045 AC01 EG08 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 7 Identification code FI theme code (reference) // H01L 21/205 F23J 15/00 J (72) Inventor Akira Baba 3 36 Takaracho, Kure City, Hiroshima Prefecture Babcock-Hitachi Kure Institute (72) Inventor Fumihiko Hanayama 6-9 Takaracho, Kure-shi, Hiroshima Babcock Hitachi Ltd. Kure Works (72) Inventor Noboru Toyama 6-9 Takara-cho, Kure-shi, Hiroshima Babcock Hitachi Stock Company Kure Office (72) Inventor Kenshi Kumagai 6-9 Takara-cho, Kure City, Hiroshima Prefecture Babcock Hitachi Co., Ltd. F-Term in Kure Factory (reference) 3K070 DA05 DA24 DA27 DA28 DA37 3K078 AA06 BA20 BA29 CA03 CA12 4D002 AA23 AA26 AC10 BA02 BA05 BA13 BA14 CA01 CA07 CA13 CA20 DA35 EA02 FA10 HA03 4K030 AA06 CA04 CA12 EA12 KA26 5F045 AC01 EG08

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 被処理ガスを燃焼分解するための燃焼炉
と、該燃焼炉の下方に設けられた、燃焼後の被処理ガス
を水冷却するための冷却部と、該冷却部の下方に設けら
れた、冷却水を受け入れるためのタンクと、該冷却部の
後流側に設けられた、該ガス中のフッ化水素を吸着する
ための湿式吸収塔とを有する燃焼式半導体排ガス処理装
置において、前記冷却部の下方に設けたタンクを前記吸
収塔下方まで延設し、前記冷却部と前記吸収塔下部との
間に、該冷却部から排出されたガスが該吸収塔下部に導
入されるように空間部を設けたことを特徴とする燃焼式
半導体排ガス処理装置。
1. A combustion furnace for combusting and decomposing a gas to be treated, a cooling unit provided below the combustion furnace for water-cooling the gas to be treated after combustion, and a cooling unit below the cooling unit. In a combustion type semiconductor exhaust gas treatment apparatus having a tank for receiving cooling water, and a wet absorption tower for adsorbing hydrogen fluoride in the gas, which is provided on the downstream side of the cooling unit A tank provided below the cooling unit is extended to below the absorption tower, and the gas discharged from the cooling unit is introduced into the lower part of the absorption tower between the cooling unit and the lower part of the absorption tower. Combustion type semiconductor exhaust gas treatment equipment characterized in that a space portion is provided as described above.
【請求項2】 前記被処理ガスがモノシランを含むもの
である、請求項1記載の燃焼式半導体排ガス処理装置。
2. The combustion type semiconductor exhaust gas treating apparatus according to claim 1, wherein the gas to be treated contains monosilane.
【請求項3】 前記吸収塔の後流側に、シリカ粉を捕集
するための、バグフィルタ式集塵装置を設けた、請求項
1または2記載の燃焼式半導体排ガス処理装置。
3. The combustion type semiconductor exhaust gas treatment apparatus according to claim 1, wherein a bag filter type dust collector for collecting silica powder is provided on the downstream side of the absorption tower.
【請求項4】 前記燃焼式半導体排ガス処理装置におい
て、前記空間部を保持するために、該タンク内の水面レ
ベルの上限を所定値以下に制御する手段を設けた、請求
項1ないし4記載の燃焼式半導体排ガス処理装置。設け
た、請求項1ないし4記載の燃焼式半導体排ガス処理装
置。
4. The combustion type semiconductor exhaust gas treating apparatus according to claim 1, further comprising means for controlling an upper limit of a water surface level in the tank to a predetermined value or less in order to hold the space portion. Combustion type semiconductor exhaust gas treatment equipment. The combustion type semiconductor exhaust gas treatment device according to claim 1, which is provided.
【請求項5】 前記燃焼式半導体排ガス処理装置におい
て、該燃焼炉の側壁(外周壁と称す)の内側に高温耐熱
性多孔物質で構成されたもう一つの側壁(内周壁と称
す)を設け、該内周壁を通して気体が燃焼炉内部に送入
されるようにしたことを特徴とする、請求項1記載の燃
焼式半導体排ガス処理装置。
5. In the combustion type semiconductor exhaust gas treating apparatus, another side wall (referred to as an inner peripheral wall) made of a high temperature heat resistant porous material is provided inside a side wall (referred to as an outer peripheral wall) of the combustion furnace, The combustion type semiconductor exhaust gas processing apparatus according to claim 1, wherein gas is introduced into the combustion furnace through the inner peripheral wall.
【請求項6】 前記燃焼式半導体排ガス処理装置におい
て、燃焼炉の外周壁と内周壁との空間が分割されてい
て、それぞれの空間へ気体送入手段を設けられているこ
とを特徴とする、請求項5記載の燃焼式半導体排ガス処
理装置。
6. The combustion type semiconductor exhaust gas treating apparatus is characterized in that a space between an outer peripheral wall and an inner peripheral wall of a combustion furnace is divided, and a gas feeding means is provided in each space. The combustion type semiconductor exhaust gas treatment device according to claim 5.
【請求項7】 前記燃焼式半導体排ガス処理装置におい
て、内周壁を通して燃焼炉内部に送入する気体が空気ま
たは窒素であることを特徴とする、請求項6記載の燃焼
式排ガス処理装置。
7. The combustion type exhaust gas treatment apparatus according to claim 6, wherein in the combustion type semiconductor exhaust gas treatment apparatus, the gas introduced into the combustion furnace through the inner peripheral wall is air or nitrogen.
JP2001216742A 2001-07-17 2001-07-17 Combustion type semiconductor exhaust gas treatment apparatus Pending JP2003024741A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001216742A JP2003024741A (en) 2001-07-17 2001-07-17 Combustion type semiconductor exhaust gas treatment apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001216742A JP2003024741A (en) 2001-07-17 2001-07-17 Combustion type semiconductor exhaust gas treatment apparatus

Publications (1)

Publication Number Publication Date
JP2003024741A true JP2003024741A (en) 2003-01-28

Family

ID=19051180

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001216742A Pending JP2003024741A (en) 2001-07-17 2001-07-17 Combustion type semiconductor exhaust gas treatment apparatus

Country Status (1)

Country Link
JP (1) JP2003024741A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006194544A (en) * 2005-01-14 2006-07-27 Japan Pionics Co Ltd Noxious gas purifying apparatus
CN100371642C (en) * 2005-09-29 2008-02-27 潘国明 Flue type dust removal and purification apparatus
WO2011162023A1 (en) * 2010-06-21 2011-12-29 エドワーズ株式会社 Gas processing system
JP2014081190A (en) * 2012-10-15 2014-05-08 Csk Inc Burner for scrubber
JP2017054862A (en) * 2015-09-07 2017-03-16 株式会社東芝 Semiconductor manufacturing device and removal device for semiconductor manufacturing device
CN112933861A (en) * 2021-01-25 2021-06-11 北京京仪自动化装备技术有限公司 Control method and equipment for waste gas treatment in semiconductor manufacturing process
KR20230096964A (en) 2020-10-30 2023-06-30 쿠리타 고교 가부시키가이샤 Exhaust gas treatment equipment

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006194544A (en) * 2005-01-14 2006-07-27 Japan Pionics Co Ltd Noxious gas purifying apparatus
JP4619798B2 (en) * 2005-01-14 2011-01-26 日本パイオニクス株式会社 Hazardous gas purification equipment
CN100371642C (en) * 2005-09-29 2008-02-27 潘国明 Flue type dust removal and purification apparatus
WO2011162023A1 (en) * 2010-06-21 2011-12-29 エドワーズ株式会社 Gas processing system
JPWO2011162023A1 (en) * 2010-06-21 2013-08-19 エドワーズ株式会社 Gas treatment system
JP2014081190A (en) * 2012-10-15 2014-05-08 Csk Inc Burner for scrubber
JP2017054862A (en) * 2015-09-07 2017-03-16 株式会社東芝 Semiconductor manufacturing device and removal device for semiconductor manufacturing device
KR20230096964A (en) 2020-10-30 2023-06-30 쿠리타 고교 가부시키가이샤 Exhaust gas treatment equipment
CN112933861A (en) * 2021-01-25 2021-06-11 北京京仪自动化装备技术有限公司 Control method and equipment for waste gas treatment in semiconductor manufacturing process

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