JP2010201358A - Exhaust gas treatment system and operation method thereof - Google Patents

Exhaust gas treatment system and operation method thereof Download PDF

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JP2010201358A
JP2010201358A JP2009050375A JP2009050375A JP2010201358A JP 2010201358 A JP2010201358 A JP 2010201358A JP 2009050375 A JP2009050375 A JP 2009050375A JP 2009050375 A JP2009050375 A JP 2009050375A JP 2010201358 A JP2010201358 A JP 2010201358A
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exhaust gas
gas treatment
treated
duct
treatment device
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JP5661249B2 (en
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Tetsuo Komai
哲夫 駒井
Toyoji Shinohara
豊司 篠原
Norihiko Nomura
典彦 野村
Yutaka Hashimoto
裕 橋本
Hideto Koriyama
日出人 郡山
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Ebara Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To fully use the treatment capacity of a treatment agent of an exhaust gas treatment apparatus as much as possible, using a centralized piping connecting structure. <P>SOLUTION: An exhaust gas treatment system includes: a plurality of exhaust gas treatment units 14a-14d including treatment tanks 40; a common inlet duct 30 into which an exhaust gas supplied to the plurality of exhaust gas treatment units flows; an outlet duct 32 for exhausting the gas treated in the exhaust gas treatment units; and a central control section 56 for controlling the operation conditions of the exhaust gas treatment units. The exhaust gas treatment system has: sections 42 installed on the downstream sides of the exhaust gas treatment units, and detecting the exhaust gas treatment capacities of the exhaust gas treatment units; outlet valves 44 installed in treated gas outflow lines 24 extending from the exhaust gas treatment units and connected to the outlet duct 32; and treated gas returning lines 46 diverged on the upstream side of the outlet valves from the treated gas outflow lines, and converged to the common inlet duct. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、排ガス処理システム及びその運転方法に係り、特に半導体装置や液晶パネル等の製造過程において排出される排ガスを処理する排ガス処理システム及びその運転方法に関する。   The present invention relates to an exhaust gas treatment system and an operation method thereof, and more particularly to an exhaust gas treatment system and an operation method thereof for treating exhaust gas discharged in a manufacturing process of a semiconductor device, a liquid crystal panel, and the like.

例えば、半導体製造産業において、エッチング装置では、エッチングガスとしてCF,CHF,C等のPFC(Perfluoro Compounds)ガスが使用され、CVD装置では、ウェーハの成膜工程でチャンバ内に付着した生成物のクリーニングガスとしてC,NF等のPFCガスが使用されている。これらのPFCガスは、温暖化係数が高く、該ガスに対する放出規制が強化されている。 For example, in the semiconductor manufacturing industry, an etching apparatus uses a PFC (Perfluoro Compounds) gas such as CF 4 , CHF 3 , or C 4 F 8 as an etching gas, and a CVD apparatus adheres to the chamber during a wafer film formation process. PFC gas such as C 2 F 6 or NF 3 is used as a cleaning gas for the obtained product. These PFC gases have a high global warming potential, and emission regulations for the gases are strengthened.

このため、図1に示すように、エッチング装置、アッシング装置またはCVD装置など半導体製造装置や液晶製造装置などの製造装置10に、排気用真空ポンプ12を介して、排ガス処理装置14を接続し、この排ガス処理装置14の処理槽(反応槽)16で排ガス中のPFCガス等を分解、除去して放出することが広く行われている。排ガス処理装置14の処理槽16の上流側の排ガス流入ライン18には圧力計20及び入口バルブ22が、下流側の処理済ガス流出ライン24には流量計26及びブロワ28がそれぞれ設置されている。   For this reason, as shown in FIG. 1, an exhaust gas treatment device 14 is connected to a manufacturing device 10 such as a semiconductor manufacturing device or a liquid crystal manufacturing device such as an etching device, an ashing device or a CVD device via an exhaust vacuum pump 12, In a treatment tank (reaction tank) 16 of the exhaust gas treatment device 14, it is widely performed to decompose, remove, and release PFC gas in the exhaust gas. A pressure gauge 20 and an inlet valve 22 are installed in the exhaust gas inflow line 18 on the upstream side of the treatment tank 16 of the exhaust gas processing apparatus 14, and a flow meter 26 and a blower 28 are installed in the processed gas outflow line 24 on the downstream side, respectively. .

半導体装置の製造においては、通常、複数の半導体製造装置が用いられている。このため、図2に示すように、複数台の半導体製造装置10からの排ガスを共通入口ダクト(集中排気ダクト)30に一旦集約し、この共通入口ダクト30にそれぞれ処理槽16を有する複数台の排ガス処理装置14の各排ガス流入ライン18を接続し、更に複数台の排ガス処理装置14の各処理済ガス流出ライン24を出口ダクト32に接続する、いわゆる集中配管接続方式を採用することも行われている。   In the manufacture of semiconductor devices, a plurality of semiconductor manufacturing devices are usually used. For this reason, as shown in FIG. 2, exhaust gases from a plurality of semiconductor manufacturing apparatuses 10 are once collected in a common inlet duct (concentrated exhaust duct) 30, and a plurality of units each having a treatment tank 16 in the common inlet duct 30. It is also possible to adopt a so-called centralized pipe connection method in which the exhaust gas inflow lines 18 of the exhaust gas treatment apparatuses 14 are connected and the processed gas outflow lines 24 of a plurality of exhaust gas treatment apparatuses 14 are connected to the outlet duct 32. ing.

図2に示す集中配管接続方式を採用した排ガス処理システムは、製造装置1台ごとに排ガス処理装置を接続するようにした、図1に示す個別接続方式を採用した排ガス処理システムと比べると、プロセスや製造装置ごとに排ガスの流量が変動したり、接続されている排ガス処理装置の稼働装置数が変化したりしても、複数の排ガス処理装置で対応するために安定した処理ができる。また、いずれかの排ガス処理装置が故障したとしても、他の排ガス処理装置を稼働させることにより、製造装置の運転を止めることなく運転を継続することができる。半導体装置や液晶パネル等の製造装置は、一般に、装置の再立上げに時間がかかり、製造装置を停止させることなく継続運転できるようにすることは重要である。   The exhaust gas treatment system adopting the centralized pipe connection method shown in FIG. 2 is a process compared to the exhaust gas treatment system adopting the individual connection method shown in FIG. Even if the flow rate of the exhaust gas fluctuates for each manufacturing apparatus or the number of operating devices of the connected exhaust gas processing apparatus changes, stable processing can be performed to cope with a plurality of exhaust gas processing apparatuses. Further, even if any exhaust gas treatment device fails, the operation can be continued without stopping the operation of the manufacturing apparatus by operating another exhaust gas treatment device. In general, a manufacturing apparatus such as a semiconductor device or a liquid crystal panel takes time to restart the apparatus, and it is important to enable continuous operation without stopping the manufacturing apparatus.

この集中配管接続方式を採用した排ガス処理システムとして、排ガス処理装置の上流に設けた流量計での測定値に基づいて流量を調整することで、各排ガス処理装置への排ガスの分散流量を一定にするようにしたものが提案されている(特許文献1参照)。   As an exhaust gas treatment system adopting this centralized pipe connection system, the flow rate of the exhaust gas to each exhaust gas treatment device is made constant by adjusting the flow rate based on the measured value with the flow meter provided upstream of the exhaust gas treatment device. The thing which made it do is proposed (refer patent document 1).

特開2005−279320号公報JP 2005-279320 A

排ガス処理装置の中で、特に排ガス中のPFCガス等を処理剤に吸着して除去するようにした乾式排ガス処理装置にあっては、処理槽(処理カラム)内の処理剤の処理能力を使い切ったら(破過したら)、新しい処理槽に交換する必要がある。例えば排ガス処理装置の下流で保証値、例えばCFが含まれる排ガスにあってはCFの除去率95%を下回ると、処理槽の交換時期(破過)と判断するようにしている。しかし、たとえCF除去率が95%を下回っても、処理槽内の処理剤の処理能力はまだ残っており、一般に高価な処理剤の処理能力を使い切ってはいなかった。 Among exhaust gas treatment equipment, especially in dry exhaust gas treatment equipment that removes PFC gas, etc. in exhaust gas by adsorbing to the treatment agent, the processing capacity of the treatment agent in the treatment tank (treatment column) is used up. Once (if it breaks through), it must be replaced with a new treatment tank. For example downstream guaranteed value of the exhaust gas treatment apparatus, for example, In the exhaust gas contains CF 4 falls below 95% rate removal of CF 4, so that it is determined that the replacement timing of the treatment tank (breakthrough). However, even if the CF 4 removal rate is less than 95%, the treatment capacity of the treatment agent in the treatment tank still remains, and generally the treatment ability of the expensive treatment agent has not been used up.

本発明は上記事情に鑑みて為されたもので、集中配管接続方式の構造を生かして、排ガス処理装置の処理剤の処理能力を可能な限り使い切ることができるようにした排ガス処理システム及びその運転方法を提供することを目的とする。   The present invention has been made in view of the above circumstances, and an exhaust gas treatment system capable of using as much as possible the treatment capacity of a treatment agent of an exhaust gas treatment device by utilizing the structure of a centralized pipe connection system and its operation It aims to provide a method.

請求項1に記載の発明は、処理槽をそれぞれ備えた複数の排ガス処理装置と、前記複数の排ガス処理装置に供給される排ガスが流入する共通入口ダクトと、前記排ガス処理装置で処理された処理済ガスを排出する出口ダクトと、前記各排ガス処理装置の運転条件を制御する集中制御部を備えた排ガス処理システムであって、前記各排ガス処理装置の下流にそれぞれ設置されて各排ガス処理装置の排ガス処理能力を検知する手段と、前記各排ガス処理装置から延びて前記出口ダクトに繋がる各処理済ガス流出ラインに設置された出口バルブと、前記出口バルブの上流側で前記処理済ガス流出ラインから分岐して前記共通入口ダクトに合流する処理済ガス戻りラインとを有することを特徴とする排ガス処理システムである。   The invention according to claim 1 is a plurality of exhaust gas treatment devices each provided with a treatment tank, a common inlet duct into which exhaust gas supplied to the plurality of exhaust gas treatment devices flows, and a treatment processed by the exhaust gas treatment device. An exhaust duct for exhausting exhaust gas and a centralized control unit for controlling the operating conditions of each exhaust gas treatment device, wherein the exhaust gas treatment system is installed downstream of each exhaust gas treatment device, Means for detecting the exhaust gas treatment capacity, an outlet valve installed in each treated gas outflow line extending from each exhaust gas treatment device and connected to the outlet duct, and from the treated gas outflow line upstream of the outlet valve An exhaust gas treatment system comprising a treated gas return line that branches and joins the common inlet duct.

これにより、複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が低下しても、該一の排ガス処理装置で処理された処理済ガスを出口ダクトから放出することなく処理済ガス戻りラインを通して共通入口ダクトに戻し、該一の排ガス処理装置を含む他の排ガス処理装置で共通入口ダクト内の排ガスを処理することで、該一の排ガス処理装置の処理槽内の処理剤の処理能力を可能な限り使い切ることができる。   As a result, even if the exhaust gas treatment capacity of one exhaust gas treatment device of a plurality of exhaust gas treatment devices is reduced, the treated gas processed by the one exhaust gas treatment device is not discharged from the outlet duct. The treatment agent in the treatment tank of the one exhaust gas treatment device is treated by returning to the common inlet duct through the return line and treating the exhaust gas in the common inlet duct with another exhaust gas treatment device including the one exhaust gas treatment device. You can use up your abilities as much as possible.

請求項2に記載の発明は、前記共通入口ダクトには、該共通入口ダクト内の圧力を検知するダクト圧力計が備えられ、前記集中制御部は、前記ダクト圧力計で測定された圧力に基づいて各排ガス処理装置に供給される排ガス流量を制御することを特徴とする請求項1に記載の排ガス処理システムである。   According to a second aspect of the present invention, the common inlet duct is provided with a duct pressure gauge for detecting the pressure in the common inlet duct, and the central control unit is based on the pressure measured by the duct pressure gauge. The exhaust gas treatment system according to claim 1, wherein the exhaust gas flow rate supplied to each exhaust gas treatment device is controlled.

このように、共通入口ダクト内の圧力に応じて、各排ガス処理装置に供給される排ガス流量を制御することにより、排ガス処理運転のための無駄な駆動力、動力の消費を抑えることができる。   Thus, wasteful driving force and power consumption for the exhaust gas treatment operation can be suppressed by controlling the exhaust gas flow rate supplied to each exhaust gas treatment device according to the pressure in the common inlet duct.

請求項3に記載の発明は、前記集中制御部とサービスサポート拠点とをLANで結んだことを特徴とする請求項1または2に記載の排ガス処理システムである。
このように、各排ガス処理装置の運転条件を制御する集中制御部とサービスサポート拠点をLAN結ぶことで、各排ガス処理装置の運転状況をサービスサポート拠点で管理して、処理槽の一元管理や、タイムリーな代替処理槽の準備、故障の予測を可能にすることができる。
A third aspect of the present invention is the exhaust gas treatment system according to the first or second aspect, wherein the central control unit and the service support base are connected by a LAN.
In this way, by connecting the centralized control unit that controls the operating conditions of each exhaust gas treatment device and the service support base via LAN, the operation status of each exhaust gas treatment equipment is managed at the service support base, and unified management of treatment tanks, It is possible to prepare a timely alternative treatment tank and predict failure.

請求項4に記載の発明は、処理槽をそれぞれ備えた複数の排ガス処理装置と、前記複数の排ガス処理装置に供給される排ガスが流入する共通入口ダクトと、前記排ガス処理装置で処理された処理済ガスを排出する出口ダクトと、前記各排ガス処理装置の運転条件を制御する集中制御部を備えた排ガス処理システムの運転方法であって、前記各排ガス処理装置の下流にそれぞれ設置された排ガス処理能力検知手段で各排ガス処理能力を検知し、前記複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が第1の所定レベルを超えた時に、該一の排ガス処理装置で処理された処理済ガスを、前記出口ダクトに流すことなく、前記共通入口ダクトに戻すことを特徴とする排ガス処理システムの運転方法である。   According to a fourth aspect of the present invention, there are provided a plurality of exhaust gas treatment devices each provided with a treatment tank, a common inlet duct into which exhaust gas supplied to the plurality of exhaust gas treatment devices flows, and a treatment processed by the exhaust gas treatment device. An exhaust gas treatment system comprising an outlet duct for exhausting exhaust gas and a centralized control unit for controlling operating conditions of each exhaust gas treatment device, wherein the exhaust gas treatment is installed downstream of each exhaust gas treatment device. Each exhaust gas treatment capability is detected by the capability detection means, and when the exhaust gas treatment capability of one of the plurality of exhaust gas treatment devices exceeds a first predetermined level, the exhaust gas treatment device is processed by the one exhaust gas treatment device. The treated gas is returned to the common inlet duct without flowing the treated gas through the outlet duct.

第1の所定レベルは、排ガス処理能力検知手段として、CFガス濃度を検知するガス検知器を用いた場合、処理剤の処理能力を使い切って処理槽の交換の基準となる、例えば50ppmである。 The first predetermined level is, for example, 50 ppm, which serves as a reference for replacing the processing tank by using up the processing capacity of the processing agent when a gas detector for detecting the CF 4 gas concentration is used as the exhaust gas processing capacity detecting means. .

請求項5に記載の発明は、前記複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が第2の所定レベルを超えた時に、該一の排ガス処理装置への排ガスの流入を停止して、該一の排ガス処理装置に備えられている処理槽を交換すべき信号を出すことを特徴とする請求項4記載の排ガス処理システムの運転方法である。   According to a fifth aspect of the present invention, when the exhaust gas treatment capability of one of the plurality of exhaust gas treatment devices exceeds a second predetermined level, the exhaust gas flows into the one exhaust gas treatment device. 5. The operation method of an exhaust gas treatment system according to claim 4, wherein the operation is stopped and a signal for exchanging the treatment tank provided in the one exhaust gas treatment device is issued.

第2の所定レベルは、排ガス処理能力検知手段として、CFガス濃度を検知するガス検知器を用いた場合、例えば200ppmであり、これにより、従来、処理能力が50ppmになった時点で交換していた処理剤の処理能力を200ppmまで引き延ばすことができる。 The second predetermined level is, for example, 200 ppm when the gas detector for detecting the CF 4 gas concentration is used as the exhaust gas processing capacity detecting means, and is replaced when the processing capacity reaches 50 ppm conventionally. The processing capacity of the treating agent that has been used can be extended to 200 ppm.

請求項6に記載の発明は、前記共通入口ダクト内の圧力をダクト圧力計で検知し、前記ダクト圧力計で測定された圧力に基づき、各排ガス処理装置に供給される排ガス流量を制御することを特徴とする請求項4または5記載の排ガス処理システムの運転方法である。   The invention according to claim 6 detects the pressure in the common inlet duct with a duct pressure gauge, and controls the exhaust gas flow rate supplied to each exhaust gas treatment device based on the pressure measured with the duct pressure gauge. A method for operating an exhaust gas treatment system according to claim 4 or 5.

請求項7に記載の発明は、前記集中制御部からのデータを、LANを通じてサービスサポート拠点に送信することを特徴とする請求項4乃至6のいずれか一項に記載の排ガス処理システムの運転方法である。   The invention according to claim 7 is a method for operating an exhaust gas treatment system according to any one of claims 4 to 6, wherein data from the central control unit is transmitted to a service support base through a LAN. It is.

本発明の排ガス処理システム及びその運転方法によれば、複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が低下しても、該一の排ガス処理装置の処理槽を排ガス処理に使用し続けることで、当該処理槽内の処理剤を可能な限り使い切ることができる。   According to the exhaust gas treatment system and the operating method of the present invention, even if the exhaust gas treatment capacity of one exhaust gas treatment device of a plurality of exhaust gas treatment devices decreases, the treatment tank of the one exhaust gas treatment device is used for exhaust gas treatment. By continuing to use, the processing agent in the processing tank can be used up as much as possible.

従来の個別接続方式を採用した排ガス処理システムの系統図である。It is a systematic diagram of an exhaust gas treatment system adopting a conventional individual connection method. 従来の集中配管接続方式を採用した排ガス処理システムの系統図である。It is a systematic diagram of an exhaust gas treatment system adopting a conventional centralized pipe connection method. 本発明の実施形態の排ガス処理システムの系統図である。1 is a system diagram of an exhaust gas treatment system according to an embodiment of the present invention. 図3に示す排ガス処理システムの処理槽の概略断面図である。It is a schematic sectional drawing of the processing tank of the waste gas processing system shown in FIG. 処理槽の他の例を示す概略断面図である。It is a schematic sectional drawing which shows the other example of a processing tank. 本発明の他の実施形態の排ガス処理システムの系統図である。It is a systematic diagram of the exhaust gas treatment system of other embodiment of this invention. 本発明の更に他の実施形態の排ガス処理システムの系統図である。It is a systematic diagram of the exhaust gas treatment system of further another embodiment of the present invention. 本発明の更に他の実施形態の排ガス処理システムの系統図である。It is a systematic diagram of the exhaust gas treatment system of further another embodiment of the present invention.

本発明の実施形態を図3乃至図8を参照して説明する。なお、図1乃至図8を通して、同一または相当する部材には同一符号を付して重複した説明を省略する。   An embodiment of the present invention will be described with reference to FIGS. 1 to 8, the same or corresponding members are denoted by the same reference numerals, and redundant description is omitted.

図3は、本発明の実施形態の排ガス処理システムを示し、図4は、図3に示す排ガス処理システムに備えられている処理槽の概略断面図を示す。図3に示すように、この排ガス処理システムには、複数の(図示では5台)の半導体製造装置等の製造装置10が接続されており、これらの製造装置10から排出されるCF等のPFCガスを含む排ガスは、真空ポンプ12を通して、共通入口ダクト30に一旦集約される。 FIG. 3 shows an exhaust gas treatment system according to an embodiment of the present invention, and FIG. 4 shows a schematic cross-sectional view of a treatment tank provided in the exhaust gas treatment system shown in FIG. As shown in FIG. 3, a plurality of (in the figure, five) semiconductor manufacturing apparatuses 10 such as semiconductor manufacturing apparatuses are connected to this exhaust gas treatment system, and CF 4 and the like discharged from these manufacturing apparatuses 10 The exhaust gas containing the PFC gas is once collected in the common inlet duct 30 through the vacuum pump 12.

共通入口ダクト30には、処理槽40をそれぞれ備えた複数(この例では4台)の排ガス処理装置14a〜14dの各排ガス流入ライン18が接続されている。この各排ガス流入ライン18には入口バルブ22が設置されている。更に、処理槽40から延びる処理済ガス流出ライン24には、流量計(または圧力計)26、ブロワ28、排ガス処理能力検知手段42及び出口バルブ44が設置されている。排ガス処理能力検知手段42として、この例では、CF等の未処理のPFCガス濃度を検出するガス検知器が用いられている。PFCガスの分解率が下がるとCOが流出してくるため、排ガス処理能力検知手段(ガス検知器)42でCO濃度を検知するようにしてもよい。排ガス処理能力検知手段としては、他に、排ガス処理に伴う処理槽の重量の変化を検知する手段が挙げられる。 The common inlet duct 30 is connected to the exhaust gas inflow lines 18 of a plurality (four in this example) of the exhaust gas treatment devices 14a to 14d each having a treatment tank 40. Each exhaust gas inflow line 18 is provided with an inlet valve 22. Further, in the treated gas outflow line 24 extending from the treatment tank 40, a flow meter (or pressure gauge) 26, a blower 28, an exhaust gas treatment capacity detecting means 42 and an outlet valve 44 are installed. In this example, a gas detector that detects the concentration of untreated PFC gas such as CF 4 is used as the exhaust gas treatment capacity detection means 42. Since CO flows out when the decomposition rate of the PFC gas decreases, the exhaust gas treatment capacity detection means (gas detector) 42 may detect the CO concentration. Other examples of the exhaust gas treatment capacity detection means include means for detecting a change in the weight of the treatment tank accompanying the exhaust gas treatment.

なお、ブロワ28の回転速度と排ガスの吸引量との関係が分かっている場合には、流量計26を省略してもよい。また、流量計26の代わりに圧力計を用いてもよい。   If the relationship between the rotation speed of the blower 28 and the suction amount of exhaust gas is known, the flow meter 26 may be omitted. A pressure gauge may be used instead of the flow meter 26.

各排ガス処理装置14a〜14dには、出口バルブ44の上流側で処理済ガス流出ライン24から分岐して共通入口ダクト30に合流する処理済ガス戻りライン46が備えられ、この処理済ガス戻りライン46には、戻りラインバルブ48及びブロア50が設置されている。このブロア50の代わりに密閉型ポンプを使用してもよい。   Each of the exhaust gas treatment devices 14a to 14d is provided with a treated gas return line 46 branched from the treated gas outflow line 24 on the upstream side of the outlet valve 44 and joined to the common inlet duct 30, and this treated gas return line. A return line valve 48 and a blower 50 are installed at 46. Instead of this blower 50, a hermetic pump may be used.

共通入口ダクト30には、該ダクト30内の圧力を検知するダクト圧力計52が設置されている。   A duct pressure gauge 52 that detects the pressure in the duct 30 is installed in the common inlet duct 30.

各排ガス処理装置14a〜14dには、流量計(または圧力計)26及び排ガス処理能力検知手段(ガス検知器)42等の信号に基づいて前記各バルブ22,32,48及びブロア28,50を制御する制御ユニット54が備えられ、この制御ユニット54及びダクト圧力計52は集中制御部としての集中制御盤56に接続されている。集中制御盤56は、LAN伝送ケーブル58を通して、サービスサポート拠点のコンピュータ60に接続されている。   Each of the exhaust gas treatment devices 14a to 14d is provided with the valves 22, 32, 48 and the blowers 28, 50 based on signals from a flow meter (or pressure gauge) 26, an exhaust gas treatment capacity detection means (gas detector) 42, and the like. A control unit 54 for controlling is provided, and the control unit 54 and the duct pressure gauge 52 are connected to a central control panel 56 as a central control unit. The central control panel 56 is connected to a computer 60 at a service support base through a LAN transmission cable 58.

各排ガス処理装置14a〜14d内に処理槽40は、図4に示すように、排ガス流入ライン18及び処理済ガス流出ライン24に接続されて排ガスと処理済ガスとの間で熱交換を行う熱交換器62と、内部にヒータ64を収納したヒータ室66と、このヒータ室66の外側に該ヒータ室66と同心状に設けら処理剤充填室68を有している。処理剤充填室68内には、処理剤70が充填されている。熱交換器62とヒータ室66は、入口側内部配管72で結ばれ、処理剤充填室68と熱交換器62は、出口側内部配管74で結ばれている。更に、処理剤充填室68及び内部配管72,74の周囲は断熱材76で覆われている。   As shown in FIG. 4, the treatment tank 40 in each of the exhaust gas treatment apparatuses 14 a to 14 d is connected to the exhaust gas inflow line 18 and the treated gas outflow line 24 to perform heat exchange between the exhaust gas and the treated gas. An exchanger 62, a heater chamber 66 in which a heater 64 is housed, and a processing agent filling chamber 68 provided concentrically with the heater chamber 66 outside the heater chamber 66 are provided. The processing agent filling chamber 68 is filled with a processing agent 70. The heat exchanger 62 and the heater chamber 66 are connected by an inlet-side internal pipe 72, and the processing agent filling chamber 68 and the heat exchanger 62 are connected by an outlet-side internal pipe 74. Further, the periphery of the processing agent filling chamber 68 and the internal pipes 72 and 74 is covered with a heat insulating material 76.

これにより、例えば25℃の排ガスは、排ガス流入ライン18を通って熱交換器62内に流入し、この熱交換器62で加熱され、ヒータ室66内を通過することで更に加熱される。そして、処理剤充填室68内に流入し該処理剤充填室68内に充填した処理剤70に接触して処理され、熱交換器62で、例えば30〜100℃、最大で140℃に冷却された後、処理済ガス流出ライン24を通って排出される。   Thus, for example, the exhaust gas at 25 ° C. flows into the heat exchanger 62 through the exhaust gas inflow line 18, is heated by the heat exchanger 62, and further heated by passing through the heater chamber 66. Then, it flows into the processing agent filling chamber 68 and is contacted with the processing agent 70 filled in the processing agent filling chamber 68 to be processed. The heat exchanger 62 cools the processing agent to, for example, 30 to 100 ° C. and a maximum of 140 ° C. After that, it is discharged through the treated gas outflow line 24.

この例では、処理剤70を700℃近くに加熱した状態で排ガスに接触させて排ガスを処理するようにしている。処理槽40内の処理剤70は、ヒータ室66内に流入したエアを加熱することにより加熱されるが、室温のエアを排ガス流入ライン18から流しつづけて処理槽40内を昇温するため、処理剤70の昇温に時間がかかる。   In this example, the exhaust gas is treated by contacting the exhaust gas in a state where the treatment agent 70 is heated to near 700 ° C. The treatment agent 70 in the treatment tank 40 is heated by heating the air that has flowed into the heater chamber 66, but the temperature of the treatment tank 40 is raised by continuously flowing air at room temperature from the exhaust gas inflow line 18. It takes time to raise the temperature of the treatment agent 70.

そこで、この例では、出口側内部配管74と入口側内部配管72とを、内部に循環バルブ78及びブロア80を設置した循環配管82で結び、更に処理済ガス流出ライン24に昇温ガス排出停止バルブ90を設け、これによって、処理槽40の昇温中に、出口側内部配管74内に流入したエアが循環配管82を通って入口側内部配管72に戻って循環するようにしている。このように、一度ヒータ室66で加熱したエアを再びヒータ室66で加熱することで、エア及び処理剤70の昇温を促進することができる。   Therefore, in this example, the outlet side internal pipe 74 and the inlet side internal pipe 72 are connected by a circulation pipe 82 in which a circulation valve 78 and a blower 80 are installed, and the temperature rising gas discharge is stopped in the treated gas outflow line 24. A valve 90 is provided so that air that has flowed into the outlet-side internal pipe 74 returns to the inlet-side internal pipe 72 through the circulation pipe 82 and circulates while the temperature of the processing tank 40 is rising. In this way, by heating the air once heated in the heater chamber 66 in the heater chamber 66 again, the temperature rise of the air and the processing agent 70 can be promoted.

なお、図4に示すように、熱交換器62で冷却される前の高温のエアが循環配管82内を流れるようにすると、循環配管82内に設置した循環バルブ78やブロア80が耐熱温度を越えてしまうことがある。そのような場合は、図5に示すように、熱交換器62の下流に、処理済ガス流出ライン24と排ガス流入ライン18を結ぶ循環配管84を設け、この循環配管84内に循環バルブ86及びブロア88を設置するようにしてもよい。   As shown in FIG. 4, when the high-temperature air before being cooled by the heat exchanger 62 flows in the circulation pipe 82, the circulation valve 78 and the blower 80 installed in the circulation pipe 82 have a heat resistant temperature. It may exceed. In such a case, as shown in FIG. 5, a circulation pipe 84 that connects the treated gas outflow line 24 and the exhaust gas inflow line 18 is provided downstream of the heat exchanger 62. A blower 88 may be installed.

この場合、処理槽40を昇温中のエアは、処理済ガス流出ライン24から循環配管84を通って排ガス流入ライン18内に流入して循環する。これによっても、処理剤70の加熱時間を短縮することができる。   In this case, the air being heated in the treatment tank 40 flows from the treated gas outflow line 24 through the circulation pipe 84 into the exhaust gas inflow line 18 and circulates. Also by this, the heating time of the processing agent 70 can be shortened.

この例では、処理剤70として、所定の組成(メディアン径(平均粒子径)55〜160μm)のAl(OH)とCa(OH)とのモル比が3:7〜5:5である混合物を430〜890℃(好ましくは580〜780℃)で十分に予め焼成したものを使用している。そして、この処理剤70を処理槽40内の処理剤充填室68内に充填し、550〜850℃(かつ、前記焼成温度よりも高い温度)でCF等のPFCガスと接触させることでPFCガスを分解し、CaFとして処理剤70に固定化するようにしている。この際に処理剤70中に含有される水分は少ない方が好ましく、5wt%以下、好ましくは3.5wt%以下、さらに好ましくは2.7wt%以下であることが好ましい。メディアン径は、一般にd50と言われ、粉体をある粒子径から2つに分けたときに、大きい側と小さい側が等量になる径のことである。この例では体積基準を用いている。実際の測定では、体積基準とした積算粒度分布曲線の50%粒度がメディアン径となる。 In this example, as the treating agent 70, a molar ratio of Al (OH) 3 and Ca (OH) 2 having a predetermined composition (median diameter (average particle diameter) of 55 to 160 μm) is 3: 7 to 5: 5. A mixture that has been sufficiently calcined at 430 to 890 ° C. (preferably 580 to 780 ° C.) is used. Then, the treatment agent 70 is filled in the treatment agent filling chamber 68 in the treatment tank 40, and brought into contact with a PFC gas such as CF 4 at 550 to 850 ° C. (and a temperature higher than the firing temperature). The gas is decomposed and fixed to the treatment agent 70 as CaF 2 . At this time, it is preferable that the moisture contained in the treatment agent 70 is small, and it is preferably 5 wt% or less, preferably 3.5 wt% or less, more preferably 2.7 wt% or less. The median diameter is generally referred to as d50, and is a diameter where the larger side and the smaller side are equivalent when the powder is divided into two from a certain particle diameter. In this example, a volume reference is used. In actual measurement, the median diameter is 50% of the integrated particle size distribution curve based on volume.

次に、この排ガス処理システムの操作例について説明する。
先ず、各排ガス処理装置14a〜14dの入口バルブ22と出口バルブ32を開き、戻りラインバルブ48を閉じた状態で、ブロア28を運転させ、各排ガス処理装置14a〜14dで排ガスを処理して処理済ガスを出口ダクト32から放出する。この時、各排ガス処理装置14a〜14dの排ガス処理能力検知手段(ガス検出器)42で検出されたガス濃度、例えば未処理のCF濃度の所定の濃度として、例えば第1規定値の50ppm以下であれば、各排ガス処理装置14a〜14dの稼働を継続する。
Next, an operation example of this exhaust gas treatment system will be described.
First, the blower 28 is operated with the inlet valve 22 and the outlet valve 32 of each of the exhaust gas treatment devices 14a to 14d open and the return line valve 48 closed, and the exhaust gas treatment devices 14a to 14d process the exhaust gas. Spent gas is discharged from the outlet duct 32. At this time, as a predetermined concentration of the gas concentration detected by the exhaust gas treatment capacity detection means (gas detector) 42 of each of the exhaust gas treatment devices 14a to 14d, for example, the untreated CF 4 concentration, for example, 50 ppm or less of the first specified value, for example. If so, the operation of each of the exhaust gas treatment devices 14a to 14d is continued.

そして、例えば1つの排ガス処理装置14aの排ガス処理能力検知手段(ガス検出器)42で検出されたガス濃度、例えばCF濃度が、例えば第1規定値の50ppm以上に達した時、従来は、排ガス処理装置14a内の処理剤70の処理性能が落ちたと判断して、処理剤交換の信号を出していた。しかし、それでも排ガス処理装置14aの処理剤70のPFCガス等の分解能力はまだあり、運転コストを考慮すると、なるべく処理剤の能力は使いきりたい。 For example, when the gas concentration detected by the exhaust gas treatment capacity detection means (gas detector) 42 of one exhaust gas treatment device 14a, for example, the CF 4 concentration reaches, for example, the first specified value of 50 ppm or more, It was determined that the processing performance of the processing agent 70 in the exhaust gas processing device 14a had deteriorated, and a signal for processing agent replacement was issued. However, there is still the ability to decompose the PFC gas or the like of the treatment agent 70 of the exhaust gas treatment device 14a, and it is desirable to use the treatment agent capacity as much as possible in consideration of operating costs.

そこで、このように、例えば排ガス処理装置14aの排ガス処理能力検知手段(ガス検出器)42で検出されたガス濃度、例えばCF濃度の所定の濃度として、例えば第1規定値の50ppm以上に達した時に、排ガス処理装置14aの処理済ガス排出ライン24の出口バルブ44を閉じて、排ガス処理装置14aで処理された処理済ガスが出口ダクト32に流入するのを阻止し、同時に戻りラインバルブ48を開き、ブロア50を運転して、排ガス処理装置14aで処理された処理済ガスを処理済ガス戻りライン46を通して共通入口ダクト30へ戻す。この場合、排ガス処理装置14aの処理剤70は、処理性能が落ちてきても、まだPFCガス等の分解能力を有している。このように、処理済のPFCガス濃度の高い排ガスを出口ダクト32側に流さずに共通入口ダクト30へ戻して、排ガス処理装置14aを含む排ガス処理装置14b〜14dで再処理することにより、排ガス処理装置14aの処理剤70の処理能力を使い切ることができる。 Thus, in this way, for example, the predetermined concentration of the gas concentration detected by the exhaust gas treatment capacity detection means (gas detector) 42 of the exhaust gas processing device 14a, for example, the CF 4 concentration, reaches, for example, the first specified value of 50 ppm or more. When this occurs, the outlet valve 44 of the processed gas discharge line 24 of the exhaust gas processing device 14a is closed to prevent the processed gas processed by the exhaust gas processing device 14a from flowing into the outlet duct 32, and at the same time the return line valve 48 And the blower 50 is operated to return the processed gas processed by the exhaust gas processing device 14 a to the common inlet duct 30 through the processed gas return line 46. In this case, the treatment agent 70 of the exhaust gas treatment device 14a still has the ability to decompose PFC gas or the like even if the treatment performance is reduced. In this way, the exhaust gas having a high PFC gas concentration that has been treated is returned to the common inlet duct 30 without flowing to the outlet duct 32 side, and is reprocessed by the exhaust gas treatment devices 14b to 14d including the exhaust gas treatment device 14a. The processing capability of the processing agent 70 of the processing apparatus 14a can be used up.

そして、例えば、排ガス処理装置14aの排ガス処理能力検知手段(ガス検出器)42で検出されたガス濃度、例えばCF濃度の所定の濃度として、例えば第2規定値の200ppm以上に達した時に、排ガス処理装置14aの処理槽40内の処理剤70が完全に破過したとみなし、排ガス処理装置14aの入口バルブ22を閉じて該排ガス処理装置14aへの排ガスの流入を停止し、排ガス処理装置14aの処理槽40を交換すべき信号を送る。そして、排ガス処理装置14aの処理済ガス戻りライン46の戻りラインバルブ48を閉じて、排ガス処理装置14aの処理槽40を交換する。 For example, when the gas concentration detected by the exhaust gas treatment capacity detection means (gas detector) 42 of the exhaust gas treatment device 14a, for example, a predetermined concentration of CF 4 concentration, for example, reaches a second specified value of 200 ppm or more, Assuming that the treatment agent 70 in the treatment tank 40 of the exhaust gas treatment device 14a has completely broken through, the inlet valve 22 of the exhaust gas treatment device 14a is closed to stop the inflow of exhaust gas into the exhaust gas treatment device 14a. The signal which should replace the processing tank 40 of 14a is sent. Then, the return line valve 48 of the treated gas return line 46 of the exhaust gas treatment device 14a is closed, and the treatment tank 40 of the exhaust gas treatment device 14a is replaced.

入口バルブ22を閉じて排ガス処理装置14aへの新たな未処理排ガスの流入を停止した時、排ガス処理装置14aをクールダウンさせる信号を送る。その場合に、共通入口ダクト30に接続された他の排ガス処理装置14b〜14dのブロア28の回転速度を上げて、排ガス処理装置一台当たりの排ガス処理量を増やす。排ガス処理装置14aの処理槽40の交換が終わり、排ガス処理装置14aの入口バルブ22を開にした情報を得たら、再び全排ガス処理装置14a〜14dでのブロア28の回転速度を均等にする。   When the inlet valve 22 is closed and the flow of new untreated exhaust gas into the exhaust gas treatment device 14a is stopped, a signal for cooling down the exhaust gas treatment device 14a is sent. In that case, the rotational speed of the blowers 28 of the other exhaust gas treatment devices 14b to 14d connected to the common inlet duct 30 is increased to increase the exhaust gas treatment amount per exhaust gas treatment device. When the replacement of the treatment tank 40 of the exhaust gas treatment device 14a is completed and the information that the inlet valve 22 of the exhaust gas treatment device 14a is opened is obtained, the rotational speed of the blower 28 in all the exhaust gas treatment devices 14a to 14d is equalized again.

次に、各排ガス処理装置14a〜14dのブロワ28の回転速度の制御について説明する。集中排気ダクト(共通入口ダクト)30に設けたダクト圧力計52の変動に基づき、各排ガス処理装置14a〜14dのブロワ28の回転速度を制御する。例えば、共通入口ダクト30内の圧力が大きくなれば、各排ガス処理装置14a〜14dのブロワ28の回転速度を上げ、逆に共通入口ダクト30内の圧力が低くなれば、各排ガス処理装置14a〜14dのブロワ28の回転速度を下げる。この場合、各排ガス処理装置14a〜14dでの処理量を均一にするため、各ブロア28は同一回転速度に制御することが好ましい。   Next, control of the rotational speed of the blower 28 of each exhaust gas treatment apparatus 14a-14d is demonstrated. Based on the fluctuation of the duct pressure gauge 52 provided in the centralized exhaust duct (common inlet duct) 30, the rotational speed of the blower 28 of each exhaust gas treatment device 14a-14d is controlled. For example, if the pressure in the common inlet duct 30 increases, the rotational speed of the blower 28 of each exhaust gas treatment device 14a-14d is increased, and conversely, if the pressure in the common inlet duct 30 decreases, each exhaust gas treatment device 14a- The rotational speed of the blower 28 of 14d is reduced. In this case, it is preferable to control each blower 28 to the same rotational speed in order to make the processing amount in each exhaust gas processing apparatus 14a-14d uniform.

例えば図3に示すように、共通入口ダクト30に4台の排ガス処理装置14a〜14dが接続されている場合、共通入口ダクト30内の圧力が極端に下がったら、4台の排ガス処理装置14a〜14d内に1台の排ガス処理装置14c、または図3に示すように、2台の排ガス処理装置14c,14dの入口バルブ22を閉めて、該1台の排ガス処理装置14c、または2台の排ガス処理装置14c,14dの運転を停止するようにしてもよい。このように、例えば2台の排ガス処理装置14c,14dの運転を停止すれば、他の2台の排ガス処理装置14a,14bの稼働で排ガスを処理できるため、排ガス処理装置の運転のための無駄な駆動力や電力を消費せずに済ますことができる。   For example, as shown in FIG. 3, when four exhaust gas treatment devices 14 a to 14 d are connected to the common inlet duct 30, if the pressure in the common inlet duct 30 is extremely reduced, the four exhaust gas treatment devices 14 a to 14 d are used. One exhaust gas treatment device 14c in 14d, or as shown in FIG. 3, the inlet valves 22 of the two exhaust gas treatment devices 14c and 14d are closed, and the one exhaust gas treatment device 14c or two exhaust gases. The operation of the processing devices 14c and 14d may be stopped. Thus, for example, if the operation of the two exhaust gas treatment devices 14c and 14d is stopped, the exhaust gas can be processed by the operation of the other two exhaust gas treatment devices 14a and 14b. Can be saved without consuming excessive driving force and power.

各排ガス処理装置への流量制御は、圧力計で圧力を測定してブロワの回転速度を制御しても、流量計で流量を測定してブロワの回転速度を制御しても良いが、流量計は、圧力損失や生成物付着/腐食に対して一般に弱い。このため、排ガス処理装置の上流側で測定する場合は、圧力計を用いて圧力を測定することが望ましい。   The flow control to each exhaust gas treatment device can be performed by controlling the blower rotation speed by measuring the pressure with a pressure gauge, or by controlling the blower rotation speed by measuring the flow rate with a flow meter. Is generally vulnerable to pressure loss and product adhesion / corrosion. For this reason, when measuring on the upstream side of the exhaust gas treatment apparatus, it is desirable to measure the pressure using a pressure gauge.

この例では、複数の排ガス処理装置14a〜14dの各制御ユニット54を集中制御盤56に接続して、複数の排ガス処理装置14a〜14dの各機器の制御を集中管理するようにしている。   In this example, the control units 54 of the plurality of exhaust gas treatment apparatuses 14a to 14d are connected to the centralized control panel 56 so that the control of each device of the plurality of exhaust gas treatment apparatuses 14a to 14d is centrally managed.

また、集中制御盤56とサービスサポート拠点のコンピュータ60とをLAN伝送ケーブル58で結び、集中制御盤56からのデータをサービスサポート拠点のコンピュータ60に伝送して、排ガス処理装置14a〜14dの運転状況をサービスサポート拠点のコンピュータ60で管理するようにしている。これにより、処理槽の一元管理や、タイムリーな代替処理槽の準備、故障の予測を可能にすることができる。   Further, the central control panel 56 and the service support base computer 60 are connected by a LAN transmission cable 58, and the data from the central control panel 56 is transmitted to the service support base computer 60, thereby operating the exhaust gas treatment apparatuses 14a to 14d. Are managed by the computer 60 at the service support base. Thereby, unified management of a processing tank, preparation of a timely alternative processing tank, and prediction of a failure can be enabled.

図6は、本発明の他の実施形態の排ガス処理システムを示す。この図6に示す例の図3に示す例と異なる点は、各排ガス処理装置14a〜14dに制御ユニット54(図3参照)を設けることなく、各排ガス処理装置14a〜14dの各センサやバルブ等を直接に集中制御盤56に接続して制御するようにしている点にある。なお、図6では、排ガス処理装置14aの各センサやバルブ等のみを集中制御盤56に接続しているが、他の排ガス処理装置14b〜14dの各センサやバルブ等も集中制御盤56に接続されている。このことは図7にあっても同様である。   FIG. 6 shows an exhaust gas treatment system according to another embodiment of the present invention. The example shown in FIG. 6 differs from the example shown in FIG. 3 in that each exhaust gas treatment device 14a-14d is not provided with a control unit 54 (see FIG. 3), and each exhaust gas treatment device 14a-14d has its respective sensors and valves. Are directly connected to the centralized control panel 56 for control. In FIG. 6, only the sensors and valves of the exhaust gas treatment device 14 a are connected to the central control panel 56, but the sensors and valves of other exhaust gas treatment devices 14 b to 14 d are also connected to the central control panel 56. Has been. The same applies to FIG.

このように集中制御盤56を独立させると、排ガス処理装置14a〜14dと集中制御盤56をそれぞれモジュールとして扱えるため、排ガス処理装置の台数が増減したり、排ガス処理装置ごとの処理プロセスが異なったりしても、その接続の増減に容易に対応できる。つまり、図3に示す例では、各排ガス処理装置14a〜14dの制御ユニット54と集中制御盤56での調整が必要であったが、図6に示す例では、各排ガス処理装置14a〜14dの各センサからのデータや駆動機器を直接集中制御盤56で制御することができる。   When the centralized control panel 56 is made independent as described above, the exhaust gas treatment devices 14a to 14d and the centralized control panel 56 can be handled as modules, respectively, so that the number of exhaust gas treatment devices can be increased or decreased, and the treatment process for each exhaust gas treatment device can be different. Even so, it is possible to easily cope with the increase or decrease of the connection. That is, in the example shown in FIG. 3, it is necessary to adjust the control unit 54 and the central control panel 56 of each exhaust gas treatment device 14a to 14d, but in the example shown in FIG. 6, each exhaust gas treatment device 14a to 14d is adjusted. Data from each sensor and driving equipment can be directly controlled by the centralized control panel 56.

図7は、本発明の更に他の実施形態の排ガス処理システムを示す。この例の図3に示す例と異なる点は、各排ガス処理装置14a〜14dの排ガスに真空ポンプ12の上流側でNガス等の希釈用ガスを供給する希釈ガス供給ライン92を備え、この希釈ガス供給ライン92に、処理済ガス流出ライン24から分岐する処理済ガス戻りライン46を合流させて、処理済ガス戻りライン46を通る処理済ガスを、真空ポンプ12の上流側から共通入口ダクト30に戻すようにした点にある。なお、図示では、排ガス処理装置14dにのみ希釈ガス供給ライン92が記載されているが、他の排ガス処理装置14a〜14cにも希釈ガス供給ライン92が備えられ、この各希釈ガス供給ライン92に各排ガス処理装置14a〜14dの各処理済ガス戻りライン46が合流するようになっている。 FIG. 7 shows an exhaust gas treatment system of still another embodiment of the present invention. This example is different from the example shown in FIG. 3 in that it includes a dilution gas supply line 92 for supplying a dilution gas such as N 2 gas upstream of the vacuum pump 12 to the exhaust gas of each of the exhaust gas treatment devices 14a to 14d. A treated gas return line 46 branched from the treated gas outflow line 24 is joined to the dilution gas supply line 92, and the treated gas passing through the treated gas return line 46 is fed from the upstream side of the vacuum pump 12 to the common inlet duct. The point is that it is set back to 30. In the drawing, the dilution gas supply line 92 is described only in the exhaust gas treatment device 14d. However, the other exhaust gas treatment devices 14a to 14c are also provided with the dilution gas supply line 92. The treated gas return lines 46 of the exhaust gas treatment devices 14a to 14d are joined together.

PFCガスは腐食性ガスではなく、また、排ガス中に腐食性ガスが含まれていても、一度処理槽40内を通っているため、処理済ガス中の腐食性ガスの大半は除去されている。このため、処理済ガスを希釈用ガスとして使用しても問題はない。   PFC gas is not corrosive gas, and even if corrosive gas is included in the exhaust gas, since it passes through the treatment tank 40 once, most of the corrosive gas in the treated gas is removed. . For this reason, even if it uses processed gas as gas for dilution, there is no problem.

真空ポンプ12を運転するため、希釈用ガスとしてのNガス等を真空ポンプ12内に流入させるようにしており、処理済ガス戻りライン42を真空ポンプ12の上流側で接続することで、Nガス等の希釈用ガスの使用量を減らし、ランニングコストを低減させることができる。 In order to operate the vacuum pump 12, N 2 gas or the like as a dilution gas is allowed to flow into the vacuum pump 12, and the treated gas return line 42 is connected to the upstream side of the vacuum pump 12, so that N The amount of the diluting gas such as 2 gas used can be reduced and the running cost can be reduced.

図8は、本発明の更に他の実施形態の排ガス処理システムを示す。この例の図6に示す例と異なる点は、処理装置10から排出される排ガスを共通入口ダクト30に送る真空ポンプ12(図6参照)を設けることなく、各排ガス処理装置14の排ガス流入ライン18に真空ポンプ12を設置して、真空ポンプ12と排ガス処理装置14を一体化した点にある。このように、本発明は、真空ポンプ一体型排ガス処理装置にも適用できる。   FIG. 8 shows an exhaust gas treatment system of still another embodiment of the present invention. This example is different from the example shown in FIG. 6 in that the exhaust gas inflow line of each exhaust gas treatment device 14 is provided without providing the vacuum pump 12 (see FIG. 6) that sends the exhaust gas discharged from the treatment device 10 to the common inlet duct 30. The vacuum pump 12 is installed at 18 and the vacuum pump 12 and the exhaust gas treatment device 14 are integrated. Thus, the present invention can also be applied to a vacuum pump integrated exhaust gas treatment apparatus.

これまで本発明の好ましい実施形態について説明したが、本発明は上述の実施形態に限定されず、その技術的思想の範囲内において種々異なる形態にて実施されてよいことは言うまでもない。   The preferred embodiments of the present invention have been described above, but the present invention is not limited to the above-described embodiments, and it goes without saying that the present invention may be implemented in various forms within the scope of the technical idea.

10 製造装置
12 真空ポンプ
14a〜14d 排ガス処理装置
18 排ガス流入ライン
22 入口バルブ
24 処理済ガス流出ライン
28,50,80,88 ブロワ
30 共通入口ダクト
32 出口ダクト
40 処理槽
42 排ガス処理能力検知手段(ガス検知器)
44 出口バルブ
46 処理済ガス戻りライン
48 戻りラインバルブ
50 ブロア
52 ダクト圧力計
54 制御ユニット
56 集中制御盤(集中制御部)
58 LAN伝送ケーブル
62 熱交換器
64 ヒータ
66 ヒータ室
68 処理剤充填室
70 処理剤
76 断熱材
78,86 循環バルブ
82,84 循環配管
DESCRIPTION OF SYMBOLS 10 Manufacturing apparatus 12 Vacuum pump 14a-14d Exhaust gas processing apparatus 18 Exhaust gas inflow line 22 Inlet valve 24 Processed gas outflow line 28,50,80,88 Blower 30 Common inlet duct 32 Outlet duct 40 Treatment tank 42 Exhaust gas processing capacity detection means ( Gas detector)
44 Outlet valve 46 Processed gas return line 48 Return line valve 50 Blower 52 Duct pressure gauge 54 Control unit 56 Central control panel (central control unit)
58 LAN transmission cable 62 heat exchanger 64 heater 66 heater chamber 68 treatment agent filling chamber 70 treatment agent 76 heat insulating material 78, 86 circulation valves 82, 84 circulation piping

Claims (7)

処理槽をそれぞれ備えた複数の排ガス処理装置と、前記複数の排ガス処理装置に供給される排ガスが流入する共通入口ダクトと、前記排ガス処理装置で処理された処理済ガスを排出する出口ダクトと、前記各排ガス処理装置の運転条件を制御する集中制御部を備えた排ガス処理システムであって、
前記各排ガス処理装置の下流にそれぞれ設置されて各排ガス処理装置の排ガス処理能力を検知する手段と、
前記各排ガス処理装置から延びて前記出口ダクトに繋がる各処理済ガス流出ラインに設置された出口バルブと、
前記出口バルブの上流側で前記処理済ガス流出ラインから分岐して前記共通入口ダクトに合流する処理済ガス戻りラインとを有することを特徴とする排ガス処理システム。
A plurality of exhaust gas treatment devices each provided with a treatment tank; a common inlet duct into which exhaust gas supplied to the plurality of exhaust gas treatment devices flows; an outlet duct for discharging treated gas treated by the exhaust gas treatment device; An exhaust gas treatment system comprising a central control unit for controlling the operating conditions of each exhaust gas treatment device,
Means for detecting the exhaust gas treatment capacity of each exhaust gas treatment device installed downstream of each exhaust gas treatment device;
An outlet valve installed in each treated gas outflow line extending from each exhaust gas treatment device and leading to the outlet duct;
An exhaust gas treatment system comprising a treated gas return line branched from the treated gas outlet line upstream of the outlet valve and joined to the common inlet duct.
前記共通入口ダクトには、該共通入口ダクト内の圧力を検知するダクト圧力計が備えられ、前記集中制御部は、前記ダクト圧力計で測定された圧力に基づいて各排ガス処理装置に供給される排ガス流量を制御することを特徴とする請求項1に記載の排ガス処理システム。   The common inlet duct is provided with a duct pressure gauge for detecting the pressure in the common inlet duct, and the central control unit is supplied to each exhaust gas treatment device based on the pressure measured by the duct pressure gauge. The exhaust gas treatment system according to claim 1, wherein the exhaust gas flow rate is controlled. 前記集中制御部とサービスサポート拠点とをLANで結んだことを特徴とする請求項1または2に記載の排ガス処理システム。   The exhaust gas treatment system according to claim 1 or 2, wherein the central control unit and a service support base are connected by a LAN. 処理槽をそれぞれ備えた複数の排ガス処理装置と、前記複数の排ガス処理装置に供給される排ガスが流入する共通入口ダクトと、前記排ガス処理装置で処理された処理済ガスを排出する出口ダクトと、前記各排ガス処理装置の運転条件を制御する集中制御部を備えた排ガス処理システムの運転方法であって、
前記各排ガス処理装置の下流にそれぞれ設置された排ガス処理能力検知手段で各排ガス処理能力を検知し、
前記複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が第1の所定レベルを超えた時に、該一の排ガス処理装置で処理された処理済ガスを、前記出口ダクトに流すことなく、前記共通入口ダクトに戻すことを特徴とする排ガス処理システムの運転方法。
A plurality of exhaust gas treatment devices each provided with a treatment tank; a common inlet duct into which exhaust gas supplied to the plurality of exhaust gas treatment devices flows; an outlet duct for discharging treated gas treated by the exhaust gas treatment device; An operation method of an exhaust gas treatment system including a central control unit that controls the operation conditions of each exhaust gas treatment device,
Each exhaust gas treatment capacity is detected by an exhaust gas treatment capacity detection means installed downstream of each exhaust gas treatment device,
When the exhaust gas treatment capability of one of the plurality of exhaust gas treatment devices exceeds a first predetermined level, the treated gas treated by the one exhaust gas treatment device is caused to flow to the outlet duct. And operating the exhaust gas treatment system by returning to the common inlet duct.
前記複数の排ガス処理装置の内の一の排ガス処理装置の排ガス処理能力が第2の所定レベルを超えた時に、該一の排ガス処理装置への排ガスの流入を停止して、該一の排ガス処理装置に備えられている処理槽を交換すべき信号を出すことを特徴とする請求項4記載の排ガス処理システムの運転方法。   When the exhaust gas treatment capability of one of the plurality of exhaust gas treatment devices exceeds a second predetermined level, the flow of the exhaust gas to the one exhaust gas treatment device is stopped, and the one exhaust gas treatment 5. The operation method of an exhaust gas treatment system according to claim 4, wherein a signal for exchanging the treatment tank provided in the apparatus is issued. 前記共通入口ダクト内の圧力をダクト圧力計で検知し、前記ダクト圧力計で測定された圧力に基づき、各排ガス処理装置に供給される排ガス流量を制御することを特徴とする請求項4または5に記載の排ガス処理システムの運転方法。   6. The pressure in the common inlet duct is detected by a duct pressure gauge, and the flow rate of exhaust gas supplied to each exhaust gas treatment device is controlled based on the pressure measured by the duct pressure gauge. A method for operating the exhaust gas treatment system according to 1. 前記集中制御部からのデータを、LANを通じてサービスサポート拠点に送信することを特徴とする請求項4乃至6のいずれか一項に記載の排ガス処理システムの運転方法。   The operation method of the exhaust gas treatment system according to any one of claims 4 to 6, wherein data from the central control unit is transmitted to a service support base through a LAN.
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