JP2004209373A - Method for starting electric discharge, treating method and treating apparatus in which the starting method is used for matter to be treated - Google Patents

Method for starting electric discharge, treating method and treating apparatus in which the starting method is used for matter to be treated Download PDF

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JP2004209373A
JP2004209373A JP2002381480A JP2002381480A JP2004209373A JP 2004209373 A JP2004209373 A JP 2004209373A JP 2002381480 A JP2002381480 A JP 2002381480A JP 2002381480 A JP2002381480 A JP 2002381480A JP 2004209373 A JP2004209373 A JP 2004209373A
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discharge
water
reaction channel
reaction
electrode
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JP4107959B2 (en
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Ryohei Itaya
良平 板谷
Mikio Deguchi
幹雄 出口
Toshihiko Toda
敏彦 戸田
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Youth Engineering Co Ltd
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Youth Engineering Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for starting electric discharge, wherein plasma can be easily generated when starting or restarting of the discharge, and a treating method and a treating apparatus in which the discharge-starting method is used. <P>SOLUTION: In the discharge starting method, a uniform water-membrane is formed in a reaction flow-path by overflowing water from the periphery of a long and narrow tubular reaction flow-path. A discharge is generated between a high voltage electrode in the air and a ground electrode in the water-membrane. When starting discharge or reignition, an electric circuit of a low resistance is formed through an electrolytic solution between the high voltage electrode and the ground electrode in the water membrane. Supply of the electrolytic solution is suspended, and the discharge of a prescribed duration or reignition is performed by breaking the current circuit between the high-voltage electrode and the ground electrode. <P>COPYRIGHT: (C)2004,JPO&NCIPI

Description

【0001】
【発明の属する技術分野】
本発明は、高圧電極と接地電極との間での放電の始動方法、この放電の始動方法を利用した被処理物の処理方法、及びこの始動方法を利用した被処理物の処理装置に関する。
【0002】
【従来の技術】
従来から、プラズマを利用してガス成分を分解して有害物質を処理する方法が提案されている。
例えば特許文献1では、対向させた電極間にガスを供給する方法が提案されている。
また特許文献2や特許文献3では、筒状のケースと、このケース内に吊り下げた放電線との間でプラズマを発生させ、このケース内にガスを供給する方法が提案されている。
しかし、上記従来のいずれの方法においても、ガスが通過する反応流路の断面全体にプラズマを発生させることは困難である。
そこで本発明者らは、反応流路を所定長さ確保し、この反応流路の軸線方向にプラズマを発生させることで、プラズマを反応流路の断面全体に形成する方法を見出した。
【0003】
【特許文献1】
特開平11−156156号公報
【特許文献2】
特開平5−15737号公報
【特許文献3】
特開平7−47224号公報
【0004】
【発明が解決しようとする課題】
しかし、反応流路の軸線方向に所定長さのプラズマを発生させるためには、始動時に高圧電極と接地電極間を接近させ、プラズマ発生後に高圧電極と接地電極を離間させなければならないが、電極間の距離を変更するための機構を設けることはコストアップとなるだけでなく、電極移動によってプラズマが不安定になってしまうという問題を有している。
【0005】
そこで、本発明は放電始動時又は再始動時に、プラズマを容易に発生させることができる放電の始動方法、この放電の始動方法を利用した被処理物の処理方法、及びこの始動方法を利用した被処理物の処理装置を提供することを目的とする。
【0006】
【課題を解決するための手段】
請求項1記載の本発明の放電の始動方法は、管状の細長い反応流路の外周から溢流することによって前記反応流路中に一様な水膜を作り、気中にある高圧電極と水膜中にある接地電極との間に放電を起こさせる放電の始動方法であって、放電の開始時又は再点弧時に、前記高圧電極と前記反応流路内の前記接地電極との間に、一旦電解液による低抵抗の電流路を形成した後に、この電解液の供給を停止して、前記高圧電極と接地電極との間の電流路を遮断することによって放電の開始または再点弧を行わせることを特徴とする。
請求項2記載の本発明の放電の始動方法は、一方に高圧電極を他方に接地電極を配置し、前記高圧電極近傍と前記接地電極との間に電流の流れる経路を形成し、放電始動時又は再始動時、前記高圧電極に電圧印加後に、前記流路中に電解液を流入させることにより、前記高圧電極と電解液の間で短い距離の放電を開始させ、前記電解液の流入を停止することにより所定長さの放電を得ることを特徴とする。
請求項3記載の本発明は、請求項1または2に記載の放電の始動方法において、アーク放電でプラズマを発生させることを特徴とする。
請求項4記載の本発明の被処理物の処理方法は、被処理物が通過する管状の細長い反応流路と、前記反応流路の上方側に配置される高圧電極と、前記反応流路の下方側に配置される接地電極とを備え、前記反応流路の軸線方向にプラズマを発生させることでフロンなどの被処理物を処理する被処理物の処理方法において、放電始動時、又は再始動時に、前記反応流路の上方側から電解液を流入させ、前記高圧電極に電圧印加後に前記電解液の流入を停止することを特徴とする。
請求項5記載の本発明は、請求項4に記載の被処理物の処理方法において、前記反応流路の外周部に水溜が形成され、前記水溜内の水を前記反応流路に供給することを特徴とする。
請求項6記載の本発明は、請求項4に記載の被処理物の処理方法において、アーク放電でプラズマを発生させることを特徴とする。
請求項7記載の本発明の被処理物の処理装置は、被処理物が通過する管状の細長い反応流路と、前記反応流路の一端側に配置される高圧電極と、前記反応流路の他端側に配置される接地電極と、前記反応流路の上方側から前記反応流路内に水を供給する給水管と、前記反応流路の下方側から前記反応流路内の水を排出する排出管と、前記反応流路の上方側から前記反応流路内に電解液を供給するノズルとを備えたことを特徴とする。
【0007】
【発明の実施の形態】
本発明の第1の実施の形態による放電の始動方法は、放電の開始時又は再点弧時に、高圧電極と反応流路内の水膜中にある接地電極との間に、一旦電解液による低抵抗の電流路を形成した後に、この電解液の供給を停止して、高圧電極と接地電極との間の電流路を遮断することによって、放電の開始または再点弧を行わせるものである。本実施の形態によれば、全く電極の移動を必要とせずに、電解液の注入によって、電極を短絡するのと同じ効果を得ることができる。すなわち、高圧電極から、若しくは、高圧電極の極近くから、電解液を反応流路内の水膜に向けて流すと、電解液の先端は水膜の水と共に降下して行き、その先端が水膜中の接地電極に達すると、水膜の電気抵抗は低くなるため、高圧電極と接地電極があたかも水膜の最上端まで移動している状態と同じになり、高圧電極から接地電極に電流が流れる。このとき直ちに電解液の注入を停止すると、高圧電極と電解液の間に誘導電圧が生じ放電が開始する。溢流する水によって、電解液は降下して行くので、あたかも接地電極を下げて行くように、放電の長さは長くなり、電解液の部分が水膜の部分から流れ去ると、所定長さの放電が得られる。電解液を高圧電極に向けて注入するときは、電極を短絡したのと同じ効果が得られることになり、いずれにしても、電極を移動させること無しで、電極を移動させたと同じ効果が得られることになる。特に水を介在させることで電解液の注入の後始末を簡単に行うことができる。
本発明の第2の実施の形態による放電の始動方法は、放電始動時又は再始動時、高圧電極に電圧印加後に、流路中に電解液を流入させることにより、高圧電極と電解液の間で短い距離の放電を開始させ、電解液の流入を停止することにより所定長さの放電を得るものである。本実施の形態によれば、放電始動時、又は再始動時に、電解液が供給されることで、高圧電極と接地電極との間には電流が流れる経路が形成されるため、プラズマを容易に発生させることができる。また、電解液の供給の停止により、高圧電極と接地電極との間には電解液が存在しなくなるが放電は継続される。
本発明の第3の実施の形態は、第1または第2の実施の形態による放電の始動方法において、アーク放電でプラズマを発生させるものである。本実施の形態によれば、より安定したプラズマを発生させることができる。
本発明の第4の実施の形態による被処理物の処理方法は、放電始動時、又は再始動時に、反応流路の上方側から電解液を流入させ、高圧電極に電圧印加後に電解液の流入を停止するものである。本実施の形態によれば、放電始動時、又は再始動時に、電解液が供給されることで、高圧電極と接地電極との間には電流が流れる経路が形成されるため、プラズマを容易に発生させることができる。また、電解液の供給の停止により、高圧電極と接地電極との間には電解液が存在しなくなるが放電は継続される。また、反応流路の長手方向にプラズマを形成することで、反応流路の断面全体にプラズマが形成されるため、被処理物は狭い断面内で長い距離を通過する間にプラズマの影響を受けるので、被処理物の分解効率が高くなる。
本発明の第5の実施の形態は、第4の実施の形態による被処理物の処理方法において、反応流路の外周部に水溜が形成され、水溜内の水を反応流路に供給するものである。本実施の形態によれば、反応流路の壁面温度が上昇しすぎることを防ぐことができるので、反応流路の途中で、反応流路内壁を流下する水が全て蒸発してしまうことを防ぐことができる。このため、反応流路内壁は常に水の膜によって覆われているので、反応流路内壁の侵食を防ぐことができる。
本発明の第6の実施の形態は、第4の実施の形態による被処理物の処理方法において、アーク放電でプラズマを発生させるものである。本実施の形態によれば、より安定したプラズマを発生させることができる。
本発明の第7の実施の形態による被処理物の処理方法は、被処理物が通過する管状の細長い反応流路と、反応流路の一端側に配置される高圧電極と、反応流路の他端側に配置される接地電極と、反応流路の上方側から反応流路内に水を供給する給水管と、反応流路の下方側から反応流路内の水を排出する排出管と、反応流路の上方側から反応流路内に電解液を供給するノズルとを備えたものである。本実施の形態によれば、プラズマの近くに水が供給されるので、排ガス中の水溶性の反応生成物を速やかに排除し、分解反応を促進させることができる。また水の流れに沿って電解液を供給することで、高圧電極と接地電極との間には電流が流れる経路が形成され、プラズマを容易に発生させることができる。また、反応流路の軸線方向にプラズマを形成することで、反応流路の断面全体にプラズマが形成されるため、排ガスは狭い断面内で長い距離を通過する間にプラズマの影響を受けるので、排ガスの分解効率が高くなる。
【0008】
【実施例】
以下本発明の一実施例による放電の始動方法について、この始動方法を適用した被処理物の処理装置及びその処理方法について説明する。
本発明で処理対象とする被処理物としては、例えば、主にハロゲン元素を含むガス、具体的には、CF(フロン14)やC(フロン318)などのPFCガス、さらにCxHyFz、CxHyClz、CxFyClz、CwFxClyBrz、SF、NF、CCl等(w、x、y、zは整数)である。また、本発明は、その他様々な有害ガスや、固体や液体の有害物質を被処理物として処理することもできる。
そして本発明の処理装置は、半導体製造用のドライエッチング装置から排出される有害物質を分解処理するプラズマ設備として適用される。また本発明は、PVD装置やCVD装置をクリーニングする場合に用いるクリーニングガスを分解処理するプラズマ処理装置としても適用される。
本発明の被処理物処理装置は、ほぼ大気圧下でプラズマ放電させる環境で使用される。また本発明の被処理物処理装置は、維持電圧の低いアーク放電を用いる。
【0009】
図1は本発明の一実施例による被処理物の処理装置の要部構成図である。
中空な本体ケース10の上部には、本体ケース10内に処理すべき排ガス等の有害物質を導入する導入パイプ17が設けられており、この導入パイプ17は、例えば粗引き用ポンプの排気管18に接続されている。
この本体ケース10の下端には、本体ケース10の内部と外部とを連通させる排出口10cが形成されている。また、本体ケース10の下端部には、排出口10c内に水を供給するための冷却水通路9が設けられている。
本体ケース10の内部において、排出口10cの上端には、所定長さの中空の反応パイプ3が鉛直に取付けられており、この反応パイプ3によって、管状又は円筒状の細長い反応流路13を構成している。この反応パイプ3の内径は、プラズマを反応流路13の断面全体に形成する上で8〜30mm程度が好ましい。特に20mm程度の内径が有害物質を効率よく処理する上で適している。またこの反応パイプ3は、パイレックス(登録商標)ガラスを用いることができるが、その他アルミナや窒化アルミニウム、窒化珪素、炭化珪素、窒化ホウ素等の絶縁体が適している。
この反応パイプ3の内部の下端部には、反応パイプ3の内面に沿って接地電極11が設けられている。この接地電極11は、例えば真鍮や銅等の導電性の高い金属が適しており、更に導電性が高く化学的に安定な、例えば金や白金等の金属がより適しているが、プラズマを発生させるという機能を発揮しうる限り、これらに限られるものではない。
【0010】
本体ケース10の上端には、先端部が白金合金の高圧電極12が設けられている。この高圧電極12の下端部は、反応パイプ3の上端近傍に配設されている。また高圧電極12の上端部は、電源14がマッチング回路15を介して接続されている。この電源14は交流高周波電源である。なお、この14が直流高圧電源の場合には、マッチング回路15は不要である。
なお高圧電極12は、反応流路13の流入側近傍で、その中心線上に配置されるが、この高圧電極12の端部を反応流路13内に挿入された状態としてもよい。
接地電極11と高圧電極12との距離は、200mm以上であることが好ましく、250mm以上であれば更に好ましい。
また本体ケース10の上端には、電解液を供給するノズル21が設けられている。電解液としては、例えばNaCl、NaOH、HSO、HNOを用いることができる。このノズル21は、高圧電極12の先端、又は反応パイプ3の上端開口部に向けて設けられている。電解液供給部22は、ノズル21から吐出させる電解液をノズル21に供給する。この電解液供給部22は、制御手段23によって供給が制御される。
また、反応パイプ3の外周と本体ケース10の内面との間には、反応パイプ3を囲むように水溜8が形成されている。本体ケース10には給水パイプ16が設けられ、この給水パイプ16は、水溜8に水を供給する。なお、水溜8に供給された水は、水溜8の上端から反応パイプ3内に供給される。
【0011】
以下に本実施例の処理装置の動作について説明する。
放電始動時、又は再始動時、制御手段23からの信号により、電解液供給部22から電解液が供給され、電解液はノズル21から吐出される。ノズル21から吐出される電解液は、高圧電極12をつたって、又は高圧電極12の下方近傍を通って反応通路13内に流下され、接地電極11を通過する。
そして電解液の供給開始後、所定時間経過後に、制御手段23からの信号によって高圧電極12に電源14から高圧電圧が印加される。連続的に滴下されている電解液によって、高圧電極12と接地電極11との間には電流が流れる経路が形成されているため、電源14から高圧電圧が印加された後に、制御手段23からの信号によって電解液供給部22からの電解液の供給は停止され、ノズル21からの電解液の吐出も停止するとプラズマは容易に発生する。
電解液の供給の停止により、高圧電極12と接地電極11との間には電解液が存在しなくなるが、放電は継続され、反応流路13の断面全体に形成されているプラズマは安定した状態で維持される。尚、高圧電極12への電圧印加のタイミングは、電解液の供給前でもよく、電解液が接地電極11まで到達した後、電解液の供給を停止する際に電圧が印加されていればよい。
【0012】
給水パイプ16から水溜8に供給される水は、反応パイプ3の上端開口部から、反応パイプ3内に供給される。反応パイプ3内に供給された水は、反応パイプ3の内壁に沿って流下し、反応パイプ3の内壁全面に水の膜を形成する。
一方被処理物は、排気管18から導入パイプ17を経由して、本体ケース10内に導入される。本体ケース10内に導入された被処理物は、反応パイプ3内を通過するときにプラズマと接触し、各ガス構成成分に分解される。このときプラズマは反応流路内の断面全体に充満しているので、ガスがプラズマ中を素通りすることがなく、効率よくガス構成成分への分解が行われる。とくに、CFを含むPFCなどのフッ素化合物は、非常に安定しているので、並の処理法は役に立たないが、プラズマに狭い空間で十分な時間接触させることで効果的に分解できる。
分解された水溶性反応生成物は、反応パイプ3の内壁に沿って流下する水に吸収される。そして分解された水溶性反応生成物は、水とともに本体ケース10外部に放出される。
【0013】
なお、高圧電極12として白金を用いることで、高圧電極12の表面を化学的に安定に保つことができる。したがって、有害物質によって高圧電極12が腐食されることを防ぐことができる。
さらに、冷却水通路9から排出口10cに水を供給すれば、反応流路13から排出される水溶性反応生成物を効率的に水に吸収させて除去することができ、しかも装置の排気側が熱によって損傷することを防ぐことができる。
なお、放電開始において、接地電極11または高圧電極12に放電開始電圧より高い電圧のパルス電圧を加えれば、パルス電圧を加えた瞬間から安定して放電をスタートさせることができる。
さらに、放電開始において、接地電極11または高圧電極12に放電開始電圧より高い電圧の高周波電圧を加えれば、安定して放電をスタートさせることができ、しかも放電開始時の印加電圧を低くすることができる。
さらに、接地電極11と高圧電極12の間に直流電圧を加えて放電させれば、接地電極11と高圧電極12との間に常に一定の電圧を加えることができるので、全時間帯にわたって放電を安定させることができる。特に、高圧電極12に負の電圧を印加すれば、放電をさらに安定させることができる。
さらに、高圧電極12はその先端部にのみ白金を使用してもよい。また、高圧電極12は、金属パイプや金属棒、またカーボン棒、Ti−Pd合金棒など、プラズマを発生させるという機能を発揮しうるものであれば特に限定はない。
【0014】
また、反応流路13の内壁全面に水の膜が形成されるので、プラズマと水とが広い面積にわたって接触する。このため、プラズマと水が接触することによって発生した水蒸気を、プラズマ中に効率よく巻き込むことができる。よって、有害物質の分解反応が促進されるとともに、水溶性反応生成物を効率的に水に吸収させることができる。よって、有害物質の分解・分離効率を高めることができる。しかも、有害物質が固体や液体の場合、有害物質を導入パイプ17を通して、または水とともに給水パイプ16から水溜8に供給し、水とともに有害物質を反応流路13の内壁に流下させれば、有害物質をプラズマと接触させて分解させることができる。
また、水溜8内の水によって反応パイプ3が冷却されるので、反応流路13の壁面温度が上昇しすぎることを防ぐことができる。このため、反応流路13の途中で、反応流路13の内壁を流下する水が全て蒸発してしまうことを防ぐことができる。したがって、反応流路13の内壁は常に水の膜によって覆われているので、反応流路13内壁の侵食を防ぐことができる。
さらに、接地電極11が反応通路13の内面に沿って設けられているので、水が接地電極11の内面に沿って流れる。このため、接地電極11が自動的に冷却され、電極の損耗を抑えることができる。しかも、有害物質は、接地電極11の内面に形成された水の膜の内側を通過するので、有害物質が反応流路13を流れるとき接地電極11が抵抗とならない。
なお、給水パイプ16から供給する水を予め加熱しておけば、プラズマの熱によって加熱された水を効率よく水蒸気とすることができるので、プラズマに水蒸気を効率よく供給することができる。
【0015】
つぎに、被処理物処理装置の他の実施形態を図2に示す。なお、図2は同実施例による処理装置の要部構成図であるが、図1と同一構成は一部図面を省略し、また同一機能には同一符号を付して説明を省略する。
この実施形態は、接地電極11を反応流路13の中心線と平行な棒状の電極としたものである。
図2に示すように、反応パイプ3の中心線、つまり反応流路13の中心線上には棒状の接地電極11が設けられている。
このため、接地電極11が、反応パイプ3の内壁に沿って流下する水によって完全に覆われてしまうことがなく、接地電極11の一部は必ず水の膜から露出している。したがって、接地電極11と高圧電極12との間に形成されたプラズマは、直接接地電極11と接することになるので、水の抵抗による電力損失をなくすことができる。
また、図2に示すように、給水パイプ16を本体ケース10の下部に設けてもよい。
【0016】
なお、上記実施例では、反応パイプ3が鉛直に取付けられたものを示したが、反応パイプ3は傾斜させたものであってもよく、高圧電極12側を上方側に、接地電極11側を下方側に配置したものであってもよい。
また、上記実施例では、反応パイプ3内に水を供給する場合で説明したが、水以外に水蒸気を供給するものであってもよい。さらに、水に、水酸化ナトリウムや水酸化カリウム、アンモニアなどのアルカリ性のものを溶解させておいてもよい。このようにすると、CFが分解してF成分が水中に溶解した際、そのままでは強い酸性になってしまうが、これを直ちに中和することができ、これにより排水系統の腐食を抑えることができるという利点がある。
また、反応生成物との反応性の高い物質(例えば、水酸化カルシウム等)を水に溶解させておいてもよい。このようにすると、CFが分解してF成分が水中に溶解した際、これを直ちに沈殿除去することができるという利点がある。
【0017】
【発明の効果】
上記実施例の説明から明らかなように、本発明によれば、放電始動時、又は再始動時に、電解液が供給されることで、高圧電極と接地電極との間には電流が流れる経路が形成されるため、プラズマを容易に発生させることができる。
【図面の簡単な説明】
【図1】本発明の一実施例による被処理物の処理装置の要部構成図
【図2】本発明の他の実施例による処理装置の要部構成図
【符号の説明】
3 反応パイプ
8 水溜
11 接地電極
12 高圧電極
13 反応流路
14 電源
16 給水パイプ
21 ノズル
22 電解液供給部
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a method for starting a discharge between a high-voltage electrode and a ground electrode, a method for treating an object using the method for starting discharge, and an apparatus for treating an object using the method for starting.
[0002]
[Prior art]
2. Description of the Related Art Conventionally, a method of treating a harmful substance by decomposing a gas component using plasma has been proposed.
For example, Patent Document 1 proposes a method of supplying a gas between opposed electrodes.
Patent Documents 2 and 3 propose a method in which plasma is generated between a cylindrical case and a discharge wire suspended in the case, and gas is supplied into the case.
However, it is difficult for any of the above-mentioned conventional methods to generate plasma over the entire cross section of the reaction channel through which the gas passes.
Therefore, the present inventors have found a method for forming a plasma over the entire cross section of the reaction channel by securing a predetermined length of the reaction channel and generating plasma in the axial direction of the reaction channel.
[0003]
[Patent Document 1]
JP-A-11-156156 [Patent Document 2]
JP-A-5-15737 [Patent Document 3]
JP-A-7-47224
[Problems to be solved by the invention]
However, in order to generate plasma of a predetermined length in the axial direction of the reaction channel, the high-voltage electrode and the ground electrode must be brought close to each other at the time of starting, and the high-voltage electrode and the ground electrode must be separated after the plasma is generated. Providing a mechanism for changing the distance between them not only increases the cost but also has the problem that the plasma becomes unstable due to the movement of the electrodes.
[0005]
Therefore, the present invention provides a method of starting a discharge that can easily generate plasma at the time of starting or restarting a discharge, a method of treating an object using the method of starting a discharge, and a method of using the method of starting. An object of the present invention is to provide a processing device for a processed product.
[0006]
[Means for Solving the Problems]
In the method for starting discharge according to the present invention, a uniform water film is formed in the reaction flow channel by overflowing from the outer periphery of the tubular elongated reaction flow channel, and the high-pressure electrode and air in the air are formed. A method for initiating a discharge that causes a discharge between a ground electrode in a film and a start of discharge or a re-ignition, between the high-voltage electrode and the ground electrode in the reaction channel. Once a low-resistance current path is formed by the electrolytic solution, the supply of the electrolytic solution is stopped, and the current path between the high-voltage electrode and the ground electrode is interrupted to start discharge or re-ignite. It is characterized by
The discharge starting method according to the present invention according to claim 2, wherein a high-voltage electrode is disposed on one side and a ground electrode is disposed on the other side, and a current flow path is formed between the vicinity of the high-voltage electrode and the ground electrode. Or, at the time of restart, after applying a voltage to the high-voltage electrode, by causing the electrolyte to flow into the flow path, a short distance discharge is started between the high-voltage electrode and the electrolyte, and the flow of the electrolyte is stopped. By doing so, a discharge of a predetermined length is obtained.
According to a third aspect of the present invention, in the discharge starting method according to the first or second aspect, plasma is generated by arc discharge.
In the method for treating an object to be treated according to the present invention, an elongated reaction channel having a tubular shape through which the object passes, a high-voltage electrode disposed above the reaction channel, A ground electrode disposed on the lower side, wherein a plasma is generated in the axial direction of the reaction channel to process the workpiece such as chlorofluorocarbons. In some cases, the electrolytic solution is caused to flow from above the reaction channel, and after the voltage is applied to the high-voltage electrode, the flowing of the electrolytic solution is stopped.
According to a fifth aspect of the present invention, in the method for treating an object to be treated according to the fourth aspect, a water reservoir is formed on an outer peripheral portion of the reaction channel, and water in the water reservoir is supplied to the reaction channel. It is characterized by.
According to a sixth aspect of the present invention, in the method for processing an object to be processed according to the fourth aspect, plasma is generated by arc discharge.
The treatment device for treating an object according to the present invention according to claim 7 is a tubular elongated reaction channel through which the object passes, a high-pressure electrode disposed at one end of the reaction channel, A ground electrode disposed on the other end side, a water supply pipe for supplying water into the reaction channel from above the reaction channel, and discharging water from the reaction channel from below the reaction channel. And a nozzle for supplying an electrolytic solution into the reaction channel from above the reaction channel.
[0007]
BEST MODE FOR CARRYING OUT THE INVENTION
The method of starting discharge according to the first embodiment of the present invention is characterized in that, at the start of discharge or at the time of re-ignition, the electrolytic solution is once interposed between the high-voltage electrode and the ground electrode in the water film in the reaction channel. After forming the low-resistance current path, the supply of the electrolytic solution is stopped, and the current path between the high-voltage electrode and the ground electrode is interrupted to start discharge or re-ignite. . According to the present embodiment, the same effect as that of short-circuiting the electrodes can be obtained by injecting the electrolytic solution without requiring any movement of the electrodes. That is, when the electrolytic solution flows toward the water film in the reaction channel from or near the high-voltage electrode, the leading end of the electrolytic solution descends together with the water in the water film, and the leading end of the electrolytic solution flows into the water film. When the water electrode reaches the ground electrode in the film, the electric resistance of the water film decreases, so that the high-voltage electrode and the ground electrode move as if they were moving to the top end of the water film, and current flows from the high-voltage electrode to the ground electrode. Flows. If the injection of the electrolytic solution is immediately stopped at this time, an induced voltage is generated between the high-voltage electrode and the electrolytic solution, and the discharge starts. The overflowing water causes the electrolyte to go down, so the discharge length becomes longer, as if the ground electrode were being lowered.When the electrolyte passed away from the water film, it reached a predetermined length. Is obtained. When the electrolyte is injected toward the high-voltage electrode, the same effect as when the electrode is short-circuited is obtained.In any case, the same effect as when the electrode is moved without moving the electrode is obtained. Will be done. In particular, the intervening water makes it easy to clean up the injection of the electrolytic solution.
The method of starting discharge according to the second embodiment of the present invention is characterized in that, at the time of starting or restarting discharge, after applying a voltage to the high-voltage electrode, the electrolytic solution is caused to flow into the flow path, so that the high-voltage electrode and the electrolytic solution are separated. To start a short-distance discharge and stop the flow of the electrolyte to obtain a discharge of a predetermined length. According to the present embodiment, when the discharge is started or restarted, the supply of the electrolytic solution forms a path through which a current flows between the high-voltage electrode and the ground electrode. Can be generated. When the supply of the electrolytic solution is stopped, the electrolytic solution no longer exists between the high-voltage electrode and the ground electrode, but the discharge is continued.
According to a third embodiment of the present invention, in the discharge starting method according to the first or second embodiment, plasma is generated by arc discharge. According to the present embodiment, more stable plasma can be generated.
In the method for treating an object to be treated according to the fourth embodiment of the present invention, at the start of discharge or at the time of restart, the electrolyte flows in from the upper side of the reaction channel, and after the voltage is applied to the high voltage electrode, the flow of the electrolyte flows. Is to stop. According to the present embodiment, when the discharge is started or restarted, the supply of the electrolytic solution forms a path through which a current flows between the high-voltage electrode and the ground electrode. Can be generated. When the supply of the electrolytic solution is stopped, the electrolytic solution no longer exists between the high-voltage electrode and the ground electrode, but the discharge is continued. In addition, since plasma is formed in the entire cross section of the reaction channel by forming plasma in the longitudinal direction of the reaction channel, the object to be processed is affected by the plasma while passing through a long distance in a narrow cross section. Therefore, the decomposition efficiency of the object to be treated increases.
According to a fifth embodiment of the present invention, there is provided a method for treating an object to be processed according to the fourth embodiment, wherein a water reservoir is formed on an outer peripheral portion of a reaction channel and water in the water reservoir is supplied to the reaction channel. It is. According to the present embodiment, it is possible to prevent the wall surface temperature of the reaction channel from excessively rising, and thus prevent the water flowing down the inner wall of the reaction channel from evaporating in the middle of the reaction channel. be able to. Therefore, since the inner wall of the reaction channel is always covered with the water film, the erosion of the inner wall of the reaction channel can be prevented.
According to a sixth embodiment of the present invention, in the method for processing an object to be processed according to the fourth embodiment, plasma is generated by arc discharge. According to the present embodiment, more stable plasma can be generated.
The method for treating an object to be processed according to the seventh embodiment of the present invention comprises a tubular elongated reaction channel through which the object passes, a high-pressure electrode disposed at one end of the reaction channel, A ground electrode disposed on the other end side, a water supply pipe for supplying water into the reaction flow path from above the reaction flow path, and a discharge pipe for discharging water from the reaction flow path from below the reaction flow path. And a nozzle for supplying an electrolytic solution into the reaction channel from above the reaction channel. According to the present embodiment, since water is supplied near the plasma, water-soluble reaction products in the exhaust gas can be quickly eliminated, and the decomposition reaction can be promoted. In addition, by supplying the electrolytic solution along the flow of water, a path through which a current flows is formed between the high-voltage electrode and the ground electrode, so that plasma can be easily generated. In addition, by forming plasma in the axial direction of the reaction flow path, plasma is formed in the entire cross section of the reaction flow path, so that the exhaust gas is affected by the plasma while passing a long distance in a narrow cross section, Exhaust gas decomposition efficiency is increased.
[0008]
【Example】
Hereinafter, a discharge starting method according to an embodiment of the present invention will be described with reference to a processing apparatus and a processing method for an object to which the starting method is applied.
The object to be treated in the present invention is, for example, a gas mainly containing a halogen element, specifically, a PFC gas such as CF 4 (Freon 14) or C 4 F 8 (Freon 318), and CxHyFz. , CxHyClz, CxFyClz, CwFxClyBrz, SF 6 , NF 3 , CCl 4 and the like (w, x, y, and z are integers). Further, the present invention can also treat various other harmful gases and solid or liquid harmful substances as objects to be treated.
The processing apparatus of the present invention is applied as a plasma facility for decomposing and processing harmful substances discharged from a dry etching apparatus for manufacturing semiconductors. The present invention is also applied to a plasma processing apparatus for decomposing a cleaning gas used for cleaning a PVD apparatus or a CVD apparatus.
The object processing apparatus of the present invention is used in an environment where plasma discharge is performed under substantially atmospheric pressure. The object processing apparatus of the present invention uses arc discharge having a low sustaining voltage.
[0009]
FIG. 1 is a main part configuration diagram of an apparatus for processing an object to be processed according to an embodiment of the present invention.
At the upper part of the hollow main body case 10, an introduction pipe 17 for introducing harmful substances such as exhaust gas to be treated into the main body case 10 is provided. This introduction pipe 17 is, for example, an exhaust pipe 18 of a roughing pump. It is connected to the.
At the lower end of the main body case 10, a discharge port 10c for communicating the inside and the outside of the main body case 10 is formed. Further, a cooling water passage 9 for supplying water into the outlet 10c is provided at a lower end portion of the main body case 10.
Inside the main body case 10, a hollow reaction pipe 3 having a predetermined length is vertically attached to the upper end of the outlet 10 c, and the reaction pipe 3 forms a tubular or cylindrical elongated reaction channel 13. are doing. The inner diameter of the reaction pipe 3 is preferably about 8 to 30 mm for forming plasma over the entire cross section of the reaction channel 13. In particular, an inner diameter of about 20 mm is suitable for efficiently processing harmful substances. In addition, Pyrex (registered trademark) glass can be used for the reaction pipe 3, but other insulators such as alumina, aluminum nitride, silicon nitride, silicon carbide, and boron nitride are suitable.
At the lower end inside the reaction pipe 3, a ground electrode 11 is provided along the inner surface of the reaction pipe 3. For the ground electrode 11, for example, a metal having high conductivity such as brass or copper is suitable, and a metal having high conductivity and being chemically stable, such as gold or platinum, is more suitable. However, the present invention is not limited to these as long as it can exhibit the function of causing
[0010]
At the upper end of the main body case 10, a high-voltage electrode 12 whose tip is made of a platinum alloy is provided. The lower end of the high-voltage electrode 12 is disposed near the upper end of the reaction pipe 3. A power supply 14 is connected to the upper end of the high-voltage electrode 12 via a matching circuit 15. The power supply 14 is an AC high-frequency power supply. When the DC power supply 14 is a DC high-voltage power supply, the matching circuit 15 is unnecessary.
Although the high-voltage electrode 12 is arranged on the center line near the inflow side of the reaction channel 13, the end of the high-voltage electrode 12 may be inserted into the reaction channel 13.
The distance between the ground electrode 11 and the high voltage electrode 12 is preferably 200 mm or more, and more preferably 250 mm or more.
Further, a nozzle 21 for supplying an electrolytic solution is provided at an upper end of the main body case 10. As the electrolytic solution, for example, NaCl, NaOH, H 2 SO 4 , HNO 3 can be used. The nozzle 21 is provided toward the tip of the high-voltage electrode 12 or the upper end opening of the reaction pipe 3. The electrolyte supply unit 22 supplies an electrolyte discharged from the nozzle 21 to the nozzle 21. The supply of the electrolytic solution supply unit 22 is controlled by the control unit 23.
A water reservoir 8 is formed between the outer periphery of the reaction pipe 3 and the inner surface of the main body case 10 so as to surround the reaction pipe 3. A water supply pipe 16 is provided in the main body case 10, and the water supply pipe 16 supplies water to the water reservoir 8. The water supplied to the water reservoir 8 is supplied into the reaction pipe 3 from the upper end of the water reservoir 8.
[0011]
Hereinafter, the operation of the processing apparatus of the present embodiment will be described.
At the start of discharge or at the time of restart, the electrolytic solution is supplied from the electrolytic solution supply unit 22 according to a signal from the control unit 23, and the electrolytic solution is discharged from the nozzle 21. The electrolytic solution discharged from the nozzle 21 flows down into the reaction passage 13 through the high voltage electrode 12 or near the lower part of the high voltage electrode 12, and passes through the ground electrode 11.
After a predetermined time has elapsed after the start of the supply of the electrolytic solution, a high voltage is applied to the high voltage electrode 12 from the power supply 14 by a signal from the control unit 23. Since a path through which a current flows is formed between the high-voltage electrode 12 and the ground electrode 11 by the continuously dropped electrolytic solution, after the high voltage is applied from the power supply 14, When the supply of the electrolyte from the electrolyte supply unit 22 is stopped by the signal and the discharge of the electrolyte from the nozzle 21 is also stopped, plasma is easily generated.
When the supply of the electrolyte is stopped, the electrolyte does not exist between the high-voltage electrode 12 and the ground electrode 11, but the discharge is continued, and the plasma formed on the entire cross section of the reaction channel 13 is in a stable state. Is maintained in. The voltage may be applied to the high-voltage electrode 12 before the supply of the electrolytic solution, or the voltage may be applied when the supply of the electrolytic solution is stopped after the electrolytic solution reaches the ground electrode 11.
[0012]
Water supplied from the water supply pipe 16 to the water reservoir 8 is supplied into the reaction pipe 3 from the upper end opening of the reaction pipe 3. The water supplied into the reaction pipe 3 flows down along the inner wall of the reaction pipe 3 and forms a water film on the entire inner wall of the reaction pipe 3.
On the other hand, the workpiece is introduced into the main body case 10 from the exhaust pipe 18 via the introduction pipe 17. The object to be treated introduced into the main body case 10 comes into contact with the plasma when passing through the inside of the reaction pipe 3 and is decomposed into respective gas components. At this time, since the plasma fills the entire cross-section in the reaction channel, the gas does not pass through the plasma, and is efficiently decomposed into gas components. In particular, a fluorine compound such as PFC containing CF 4 is very stable, so that an ordinary treatment method is useless, but it can be effectively decomposed by contacting the plasma with a narrow space for a sufficient time.
The decomposed water-soluble reaction product is absorbed by water flowing down along the inner wall of the reaction pipe 3. The decomposed water-soluble reaction product is released to the outside of the main body case 10 together with water.
[0013]
By using platinum as the high voltage electrode 12, the surface of the high voltage electrode 12 can be kept chemically stable. Therefore, it is possible to prevent the high-voltage electrode 12 from being corroded by harmful substances.
Further, if water is supplied from the cooling water passage 9 to the discharge port 10c, the water-soluble reaction products discharged from the reaction flow path 13 can be efficiently absorbed and removed by water, and the exhaust side of the apparatus is reduced. Damage due to heat can be prevented.
At the start of the discharge, if a pulse voltage higher than the discharge start voltage is applied to the ground electrode 11 or the high voltage electrode 12, the discharge can be started stably from the moment the pulse voltage is applied.
Further, at the start of discharge, if a high-frequency voltage higher than the discharge start voltage is applied to the ground electrode 11 or the high-voltage electrode 12, the discharge can be started stably, and the applied voltage at the start of discharge can be reduced. it can.
Furthermore, if a DC voltage is applied between the ground electrode 11 and the high-voltage electrode 12 to cause a discharge, a constant voltage can always be applied between the ground electrode 11 and the high-voltage electrode 12, so that the discharge is performed over the entire time period. Can be stabilized. In particular, when a negative voltage is applied to the high voltage electrode 12, the discharge can be further stabilized.
Further, the high voltage electrode 12 may use platinum only at the tip. The high-voltage electrode 12 is not particularly limited as long as it can exert a function of generating plasma, such as a metal pipe, a metal rod, a carbon rod, or a Ti-Pd alloy rod.
[0014]
In addition, since a water film is formed on the entire inner wall of the reaction channel 13, the plasma and water come into contact over a wide area. Therefore, the water vapor generated by the contact between the plasma and the water can be efficiently involved in the plasma. Therefore, the decomposition reaction of the harmful substance is promoted, and the water-soluble reaction product can be efficiently absorbed in water. Therefore, the efficiency of decomposing and separating harmful substances can be increased. Moreover, when the harmful substance is a solid or a liquid, the harmful substance is supplied to the water reservoir 8 through the introduction pipe 17 or together with the water from the water supply pipe 16, and the harmful substance flows down to the inner wall of the reaction channel 13 together with the water. The substance can be decomposed by contact with the plasma.
Further, since the reaction pipe 3 is cooled by the water in the water reservoir 8, it is possible to prevent the wall surface temperature of the reaction channel 13 from excessively increasing. For this reason, it is possible to prevent the water flowing down the inner wall of the reaction channel 13 from being completely evaporated in the middle of the reaction channel 13. Therefore, since the inner wall of the reaction channel 13 is always covered with the water film, erosion of the inner wall of the reaction channel 13 can be prevented.
Further, since the ground electrode 11 is provided along the inner surface of the reaction passage 13, water flows along the inner surface of the ground electrode 11. Therefore, the ground electrode 11 is automatically cooled, and the wear of the electrode can be suppressed. Moreover, the harmful substance passes through the inside of the water film formed on the inner surface of the ground electrode 11, so that the ground electrode 11 does not become a resistance when the harmful substance flows through the reaction channel 13.
In addition, if the water supplied from the water supply pipe 16 is heated in advance, the water heated by the heat of the plasma can be efficiently converted into steam, so that the steam can be efficiently supplied to the plasma.
[0015]
Next, another embodiment of the object processing apparatus is shown in FIG. Although FIG. 2 is a configuration diagram of a main part of the processing apparatus according to the embodiment, the same configuration as FIG. 1 is partially omitted from the drawings, and the same functions are denoted by the same reference numerals and description thereof is omitted.
In this embodiment, the ground electrode 11 is a rod-shaped electrode parallel to the center line of the reaction channel 13.
As shown in FIG. 2, a rod-shaped ground electrode 11 is provided on the center line of the reaction pipe 3, that is, on the center line of the reaction channel 13.
For this reason, the ground electrode 11 is not completely covered with the water flowing down along the inner wall of the reaction pipe 3, and a part of the ground electrode 11 is always exposed from the water film. Therefore, the plasma formed between the ground electrode 11 and the high-voltage electrode 12 comes into direct contact with the ground electrode 11, so that power loss due to water resistance can be eliminated.
Further, as shown in FIG. 2, the water supply pipe 16 may be provided at a lower portion of the main body case 10.
[0016]
In the above-described embodiment, the reaction pipe 3 is vertically mounted. However, the reaction pipe 3 may be inclined, and the high-voltage electrode 12 is on the upper side and the ground electrode 11 is on the ground. It may be arranged on the lower side.
Further, in the above-described embodiment, the case where water is supplied into the reaction pipe 3 has been described, but water other than water may be supplied. Further, an alkaline substance such as sodium hydroxide, potassium hydroxide, or ammonia may be dissolved in water. In this way, when CF 4 is decomposed and the F component is dissolved in water, it becomes strongly acidic as it is, but this can be immediately neutralized, thereby suppressing the corrosion of the drainage system. There is an advantage that you can.
Further, a substance having high reactivity with the reaction product (for example, calcium hydroxide or the like) may be dissolved in water. This has the advantage that when the CF 4 is decomposed and the F component is dissolved in water, it can be immediately precipitated and removed.
[0017]
【The invention's effect】
As is clear from the description of the above embodiment, according to the present invention, at the time of starting discharge or at the time of restart, by supplying the electrolyte, a path through which a current flows between the high-voltage electrode and the ground electrode is formed. Since it is formed, plasma can be easily generated.
[Brief description of the drawings]
FIG. 1 is a main part configuration diagram of an apparatus for processing an object to be processed according to one embodiment of the present invention. FIG. 2 is a main part configuration diagram of a processing apparatus according to another embodiment of the present invention.
3 Reaction pipe 8 Water reservoir 11 Ground electrode 12 High voltage electrode 13 Reaction channel 14 Power supply 16 Water supply pipe 21 Nozzle 22 Electrolyte supply part

Claims (7)

管状の細長い反応流路の外周から溢流することによって前記反応流路中に一様な水膜を作り、気中にある高圧電極と水膜中にある接地電極との間に放電を起こさせる放電の始動方法であって、放電の開始時又は再点弧時に、前記高圧電極と前記反応流路内の水膜中にある接地電極との間に、一旦電解液による低抵抗の電流路を形成した後に、この電解液の供給を停止して、前記高圧電極と接地電極との間の電流路を遮断することによって、所定長さの放電の開始または再点弧を行わせることを特徴とする放電の始動方法。A uniform water film is formed in the reaction channel by overflowing from the outer periphery of the tubular elongated reaction channel, and a discharge is caused between the high-pressure electrode in the air and the ground electrode in the water film. A method for starting discharge, wherein at the start of discharge or at the time of re-ignition, a low-resistance current path is once passed between the high-voltage electrode and the ground electrode in the water film in the reaction channel by an electrolytic solution. After the formation, the supply of the electrolytic solution is stopped, and a current path between the high-voltage electrode and the ground electrode is interrupted to start or re-ignite a predetermined length of discharge. How to start the discharge. 一方に高圧電極を他方に接地電極を配置し、前記高圧電極近傍と前記接地電極との間に電流の流れる経路を形成し、放電始動時又は再始動時、前記高圧電極に電圧印加後に、前記流路中に電解液を流入させることにより、前記高圧電極と電解液の間で短い距離の放電を開始させ、前記電解液の流入を停止することにより所定長さの放電を得ることを特徴とする放電の始動方法。A high-voltage electrode is disposed on one side and a ground electrode is disposed on the other side, and a current flow path is formed between the vicinity of the high-voltage electrode and the ground electrode, at the time of starting or restarting discharge, after applying a voltage to the high-voltage electrode, By flowing an electrolytic solution into the flow path, a short-distance discharge is started between the high-voltage electrode and the electrolytic solution, and a predetermined length of discharge is obtained by stopping the flow of the electrolytic solution. How to start the discharge. アーク放電でプラズマを発生させることを特徴とする請求項1または2に記載の放電の始動方法。3. The method according to claim 1, wherein the plasma is generated by an arc discharge. 被処理物が通過する管状の細長い反応流路と、前記反応流路の上方側に配置される高圧電極と、前記反応流路の下方側に配置される接地電極とを備え、前記反応流路の軸線方向にプラズマを発生させることでフロンなどの被処理物を処理する被処理物の処理方法において、放電始動時、又は再始動時に、前記反応流路の上方側から電解液を流入させ、前記高圧電極に電圧印加後に前記電解液の流入を停止することを特徴とする被処理物の処理方法。An elongate tubular reaction channel through which the object passes, a high-pressure electrode disposed above the reaction channel, and a ground electrode disposed below the reaction channel; In the processing method of the object to be processed by processing the object such as chlorofluorocarbons by generating plasma in the axial direction, at the start of discharge, or at the time of restart, the electrolytic solution flows from the upper side of the reaction channel, A method for treating an object to be treated, wherein the flow of the electrolytic solution is stopped after a voltage is applied to the high-voltage electrode. 前記反応流路の外周部に水溜が形成され、前記水溜内の水を前記反応流路に供給することを特徴とする請求項4に記載の被処理物の処理方法。The method according to claim 4, wherein a water reservoir is formed at an outer peripheral portion of the reaction channel, and water in the water reservoir is supplied to the reaction channel. アーク放電でプラズマを発生させることを特徴とする請求項4に記載の被処理物の処理方法。The method according to claim 4, wherein plasma is generated by arc discharge. 被処理物が通過する管状の細長い反応流路と、前記反応流路の一端側に配置される高圧電極と、前記反応流路の他端側に配置される接地電極と、前記反応流路の上方側から前記反応流路内に水を供給する給水管と、前記反応流路の下方側から前記反応流路内の水を排出する排出管と、前記反応流路の上方側から前記反応流路内に電解液を供給するノズルとを備えたことを特徴とする被処理物の処理装置。A tubular elongated reaction channel through which an object passes, a high-pressure electrode disposed at one end of the reaction channel, a ground electrode disposed at the other end of the reaction channel, A water supply pipe for supplying water into the reaction flow path from above, a discharge pipe for discharging water from the reaction flow path from below the reaction flow path, and a reaction flow from above the reaction flow path And a nozzle for supplying an electrolytic solution in the passage.
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