JPH10220832A - Safety device - Google Patents

Safety device

Info

Publication number
JPH10220832A
JPH10220832A JP9020484A JP2048497A JPH10220832A JP H10220832 A JPH10220832 A JP H10220832A JP 9020484 A JP9020484 A JP 9020484A JP 2048497 A JP2048497 A JP 2048497A JP H10220832 A JPH10220832 A JP H10220832A
Authority
JP
Japan
Prior art keywords
gas
reaction
ejector
exhaust
nitrogen
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.)
Granted
Application number
JP9020484A
Other languages
Japanese (ja)
Other versions
JP3801286B2 (en
Inventor
Kenichiro Kosaka
健一郎 小阪
Yasuhiro Yamauchi
康弘 山内
Akito Komori
明人 小森
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP02048497A priority Critical patent/JP3801286B2/en
Publication of JPH10220832A publication Critical patent/JPH10220832A/en
Application granted granted Critical
Publication of JP3801286B2 publication Critical patent/JP3801286B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Abstract

PROBLEM TO BE SOLVED: To emit reaction gas to the outside of a system at a sufficiently low concentration without using an expensive, large-sized maintenance power source, and to maintain the internal pressure of a container at an atmospheric pressure or less. SOLUTION: A safety device is equipped with a reaction container 11 to which stock and process gas are fed from a stock feeder to provide a reaction inside, an exhauster 13 which is connected with the reaction container 11 and exhausts the gas inside the reaction container 11, an eliminator 14 which eliminates a deleterious ingredient contained in the exhaust air in the exhauster 13, an ejector 20 which is connected to the line between the reaction container 11 and exhauster 13 to dilute the exhaust air and gas from the reaction container 11, and a nitrogen feeder 25 connected with the ejector. In the normal operation, the reaction container 11 is exhausted by means of the exhauster 13, and deleterious gas is eliminated by means of the eliminator 14 to be exhausted. In the emergency operation, nitrogen is fed to the ejector 20 from the nitrogen feeder 25 to generate the negative pressure at the throat part of the ejector 20 by the flow of nitrogen, thus exhausting the reaction gas from the reaction container 11.

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】本発明は安全装置に関し、特
に有害ガスや高温ガスを用いる設備の、緊急停止時の排
気設備に使用される安全装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a safety device, and more particularly, to a safety device used for an exhaust system at the time of an emergency stop of a facility using toxic gas or high-temperature gas.

【0002】[0002]

【従来の技術】従来、反応容器の排気装置の例として
は、図2に示すものが知られている。図中の付番1は反
応容器である。この反応容器1には、該反応容器1に原
料及びプロセスガスが供給される原料供給装置2が接続
され、反応容器1内で反応が行われる。なお、前記原料
供給装置2は、インタロック装置により非常時には原料
の供給が自動的に停止されるようになっている。前記反
応容器1には、排気装置3,除害装置4,ベントスタッ
ク5などの排気設備が順次接続されている。前記反応容
器1における反応生成物及びプロセスガスに有害成分が
含まれている場合は、前記排気装置3により内部のガス
を排気し、前記除害装置4にて排気に含まれる有害成分
を取り除いた後、ベントスタック5から大気に放出され
る。ここで、前記排気装置3は、反応容器1内部の排気
を行うとともに、反応容器1内を大気圧以下に保って、
反応容器1から外部への漏洩を防止する機能を有する。
2. Description of the Related Art FIG. 2 shows an example of a conventional exhaust device for a reaction vessel. Reference numeral 1 in the figure denotes a reaction vessel. The reaction vessel 1 is connected to a raw material supply device 2 for supplying a raw material and a process gas to the reaction vessel 1, and a reaction is performed in the reaction vessel 1. In the raw material supply device 2, the supply of the raw material is automatically stopped in an emergency by an interlock device. Exhaust equipment such as an exhaust device 3, an abatement device 4, and a vent stack 5 are sequentially connected to the reaction vessel 1. When a harmful component is contained in the reaction product and the process gas in the reaction vessel 1, the internal gas is exhausted by the exhaust device 3, and the harmful component contained in the exhaust gas is removed by the abatement device 4. Thereafter, the gas is released from the vent stack 5 to the atmosphere. Here, the exhaust device 3 exhausts the inside of the reaction vessel 1 and maintains the inside of the reaction vessel 1 at an atmospheric pressure or less.
It has a function of preventing leakage from the reaction vessel 1 to the outside.

【0003】前記反応容器1と排気装置3を接続するラ
イン、及び除害装置4とベントスタック5を結ぶライン
間は、予備排気装置6,予備除害装置7を介装したライ
ン8により接続されている。これら予備排気装置6及び
予備除害装置7は、前記排気装置3及び除害装置4の故
障時にバックアップを行うために設置されている。前記
排気装置3,除害装置4,予備排気装置6及び予備除害
装置7には、停電時にもこれらの各装置が駆動するよう
に、無停電電源等の保安電源9が接続されている。
A line connecting the reaction vessel 1 and the exhaust device 3 and a line connecting the abatement device 4 and the vent stack 5 are connected by a line 8 having a preliminary exhaust device 6 and a preliminary abatement device 7 interposed therebetween. ing. The preliminary exhaust device 6 and the preliminary abatement device 7 are installed to provide backup when the exhaust device 3 and the abatement device 4 fail. A safety power supply 9 such as an uninterruptible power supply is connected to the exhaust device 3, the abatement device 4, the preliminary exhaust device 6, and the preliminary abatement device 7 so that these devices are driven even during a power failure.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、従来の
反応容器の排気装置においては、排気装置3,除害装置
4,予備排気装置6及び予備除害装置7を駆動するため
の無停電電源等の保安電源9は大型でかつ高価であると
ともに、保守,点検等を必要とする。また、機械的な駆
動部を含む除害装置,排気装置の信頼性を確保するた
め、バックアップが必要である。
However, in the conventional exhaust apparatus for a reaction vessel, the exhaust apparatus 3, the abatement apparatus 4, the preliminary exhaust apparatus 6, and the uninterruptible power supply for driving the preliminary abatement apparatus 7 are provided. The security power supply 9 is large and expensive, and requires maintenance and inspection. In addition, a backup is required to ensure the reliability of the abatement device and the exhaust device including the mechanical drive unit.

【0005】本発明はこうした事情を考慮してなされた
もので、反応容器からの排気と反応ガスの希釈を行うエ
ゼクタを反応容器と排気装置を結ぶラインに接続するよ
うに設け、非常運転時にこのエゼクタを用いることによ
り、従来のように大型で高価な保守電源を用いることな
く、反応容器からの排気と反応ガスの希釈を行い、反応
ガスを十分に低い濃度で系外に放出できるとともに、反
応容器の内圧を大気圧以下に保持できる安全装置を提供
することを目的とする。
The present invention has been made in view of such circumstances, and an ejector for exhausting a reaction vessel and diluting a reaction gas is provided so as to be connected to a line connecting the reaction vessel and an exhaust device. By using an ejector, it is possible to exhaust the reaction vessel and dilute the reaction gas without using a large and expensive maintenance power source as in the past, and discharge the reaction gas out of the system at a sufficiently low concentration. An object of the present invention is to provide a safety device capable of maintaining the internal pressure of a container at or below atmospheric pressure.

【0006】[0006]

【課題を解決するための手段】この発明は、原料供給装
置から原料及びプロセスガスが供給され、内部で反応が
行われる反応容器と、この反応容器に接続され、該反応
容器内部のガスを排気する排気装置と、この排気装置に
接続され、該排気装置内の排気に含まれる有害成分を取
り除く除害装置と、前記反応容器と排気装置を結ぶライ
ンに接続され、前記反応容器からの排気とガスの希釈を
行うエゼクタと、このエゼクタに接続された窒素供給装
置とを具備し、通常運転時は、反応容器内を排気装置に
より排気し、除外装置により有害ガスを取り除いた後排
気し、非常運転時は、窒素供給装置から窒素をエゼクタ
に供給して、窒素の流動によりエゼクタの喉部に負圧を
発生させることにより、反応容器から反応ガスを排気す
ることを特徴とする安全装置である。
SUMMARY OF THE INVENTION According to the present invention, there is provided a reaction vessel in which a raw material and a process gas are supplied from a raw material supply device and a reaction is carried out therein, and a gas connected to the reaction vessel and exhausting the gas inside the reaction vessel. Exhaust device, an abatement device connected to the exhaust device for removing harmful components contained in exhaust gas in the exhaust device, and an exhaust device connected to a line connecting the reaction container and the exhaust device, and exhaust gas from the reaction container. An ejector for diluting gas and a nitrogen supply device connected to the ejector are provided. During normal operation, the inside of the reaction vessel is evacuated by an exhaust device, and after removing harmful gas by an exclusion device, exhaust is performed. During operation, the reaction gas is exhausted from the reaction vessel by supplying nitrogen to the ejector from the nitrogen supply device and generating a negative pressure in the throat of the ejector by the flow of nitrogen. It is a safety device.

【0007】(作用) i)液体窒素タンクを用いた窒素供給装置は動力を用いる
ことなく、安定して窒素ガスを供給することができ、停
電時でも反応ガスの排気と希釈を行うことができる。
(Operation) i) A nitrogen supply device using a liquid nitrogen tank can supply nitrogen gas stably without using power, and can exhaust and dilute the reaction gas even during a power failure. .

【0008】ii) エゼクタを用いることにより、希釈用
の窒素の供給のみで機械駆動を行うことなく、排気系を
構成でき、電力なしで反応容器内の圧力を大気圧以下に
保つことができる。iii)エゼクタ,液体窒素タンクを用
いた窒素供給系統を非常時のバックアップの設備とする
ことにより、設備を簡略化できる。
Ii) By using an ejector, an exhaust system can be configured without mechanical driving only by supplying nitrogen for dilution, and the pressure in the reaction vessel can be maintained at or below atmospheric pressure without power. iii) The equipment can be simplified by using a nitrogen supply system using an ejector and a liquid nitrogen tank as backup equipment in an emergency.

【0009】[0009]

【発明の実施の形態】以下、本発明の一実施例に係る安
全装置を図1を参照して説明する。図中の付番11は反応
容器である。この反応容器11には、該反応容器11に原料
及びプロセスガスが供給される原料供給装置12が接続さ
れ、反応容器11内で反応が行われる。なお、前記原料供
給装置12は、インタロック装置により非常時には原料の
供給が自動的に停止されるようになっている。前記反応
容器11には、排気装置13,除害装置14,ベントスタック
15などの排気設備が順次接続されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A safety device according to one embodiment of the present invention will be described below with reference to FIG. Reference number 11 in the figure is a reaction vessel. The reaction vessel 11 is connected to a raw material supply device 12 for supplying a raw material and a process gas to the reaction vessel 11, and a reaction is performed in the reaction vessel 11. In addition, in the raw material supply device 12, the supply of the raw material is automatically stopped in an emergency by an interlock device. The reaction vessel 11 includes an exhaust device 13, an abatement device 14, a vent stack
Exhaust facilities such as 15 are connected sequentially.

【0010】前記反応容器11と排気装置13を結ぶライン
16には、排気流量調節弁17,容器排気系閉鎖弁18を順次
介装したライン19を介してエゼクタ20が接続されてい
る。ここで、排気流量調節弁17は反応容器11からの排気
流量を調節するものである。前記エゼクタ20には、エゼ
クタ20側から順にノーマルオープンである電磁弁21,窒
素流量調節弁22及び減圧弁23を介装したライン24を介し
て窒素供給装置25が接続されている。ここで、窒素流量
調節弁22は窒素の流量を、減圧弁23は窒素の圧力を調節
するものである。また、電磁弁21は通常運転時は閉じら
れ、非常時は開放されている。
A line connecting the reaction vessel 11 and the exhaust device 13
An ejector 20 is connected to 16 via a line 19 in which an exhaust flow control valve 17 and a container exhaust system closing valve 18 are sequentially provided. Here, the exhaust flow rate control valve 17 adjusts the exhaust flow rate from the reaction vessel 11. A nitrogen supply device 25 is connected to the ejector 20 via a line 24 in which a normally open solenoid valve 21, a nitrogen flow control valve 22, and a pressure reducing valve 23 are interposed in this order from the ejector 20 side. Here, the nitrogen flow control valve 22 controls the flow rate of nitrogen, and the pressure reducing valve 23 controls the pressure of nitrogen. The solenoid valve 21 is closed during normal operation, and is opened during an emergency.

【0011】このように、上記実施例に係る安全装置
は、原料供給装置12に接続された反応容器11と、前記反
応容器11に順次接続された排気装置13,除害装置14及び
ベントスタック15と、前記反応容器11と排気装置13を結
ぶライン16に接続された排気流量調節弁17,容器排気系
閉鎖弁18及びエゼクタ20と、このエゼクタ20に接続され
た電磁弁21,窒素流量調節弁22,減圧弁23及び窒素供給
装置25とを具備した構成となっている。かかる構成の安
全装置の通常運転時,停電等の非常時における作用は、
以下の通りである。
As described above, the safety device according to the above embodiment includes a reaction vessel 11 connected to a raw material supply device 12, an exhaust device 13, a detoxification device 14, and a vent stack 15 sequentially connected to the reaction container 11. An exhaust flow control valve 17, a container exhaust system closing valve 18, and an ejector 20 connected to a line 16 connecting the reaction vessel 11 and the exhaust device 13, an electromagnetic valve 21, a nitrogen flow control valve connected to the ejector 20, 22, a pressure reducing valve 23 and a nitrogen supply device 25 are provided. The operation of the safety device having such a configuration during normal operation and during an emergency such as a power failure
It is as follows.

【0012】i)通常運転時:反応容器11を排気装置13に
より排気し、除害装置14を用いて有害ガスを取り除いた
後、ベントスタック15により排気する。 ii) 非常時:原料供給装置12は、インタロック装置によ
り自動的に原料の供給が停止される。電磁弁21はノーマ
ルオープンであるので、非常時には自動的に開放され
る。電磁弁21が開くことにより、窒素供給装置25から窒
素が減圧弁23,窒素流量調節弁22,電磁弁21を通ってエ
ゼクタ20に供給される。窒素の流動によりエゼクタ20の
喉部に負圧が発生し、反応容器11から反応ガスを排気す
る。なお、窒素中の排気ガスの濃度を低く抑えるため
に、窒素の圧力は減圧弁23、窒素の流量は窒素流量調節
弁22、反応容器11からの排気流量は排気流量調節弁17を
用いて予め調節しておく。前記容器排気系閉鎖弁18は、
ノーマルオープンの電磁弁21で通常運転時は“閉”とし
て、エゼクタ20へのラインを閉じておくが、非常時は開
放され、エゼクタ20への排気ラインを開放する。
I) During normal operation: The reaction vessel 11 is evacuated by the exhaust device 13, harmful gas is removed using the abatement device 14, and then exhausted by the vent stack 15. ii) Emergency: The raw material supply device 12 automatically stops supplying the raw material by the interlock device. Since the solenoid valve 21 is normally open, it is automatically opened in an emergency. When the solenoid valve 21 is opened, nitrogen is supplied from the nitrogen supply device 25 to the ejector 20 through the pressure reducing valve 23, the nitrogen flow control valve 22, and the solenoid valve 21. A negative pressure is generated in the throat of the ejector 20 by the flow of the nitrogen, and the reaction gas is exhausted from the reaction vessel 11. In order to keep the concentration of exhaust gas in nitrogen low, the pressure of nitrogen is reduced in advance by using a pressure reducing valve 23, the flow rate of nitrogen is controlled in advance by a nitrogen flow control valve 22, and the flow rate of exhaust from the reaction vessel 11 is controlled in advance by using an exhaust flow rate control valve 17. Adjust it. The container exhaust system closing valve 18 includes:
The line to the ejector 20 is kept closed during normal operation with the normally open solenoid valve 21, but is opened in an emergency, and the exhaust line to the ejector 20 is opened.

【0013】上記実施例に係る安全装置によれば、以下
に述べる効果を有する。まず、エゼクタ20は窒素流量が
確保されれば、喉部に負圧が発生し、反応容器11から反
応ガスを吸い出すことができる。また、エゼクタ20を駆
動する時は、駆動用の窒素が窒素供給装置25からエゼク
タ20に供給されているため、窒素の流量と排ガスの流量
を予め調整しておくことで、反応ガスを希釈し下流の濃
度を低く抑えることができる。更に、ノーマルオープン
の電磁弁21を用いることにより、停電時は自動的にエゼ
クタ20の駆動と非常用の排気ラインが開放されるため、
別途、停電対策を行うことなく、排気を行うことができ
る。
The safety device according to the above embodiment has the following effects. First, if the nitrogen flow rate is secured in the ejector 20, a negative pressure is generated in the throat and the reaction gas can be sucked out of the reaction vessel 11. When the ejector 20 is driven, since the driving nitrogen is supplied to the ejector 20 from the nitrogen supply device 25, the reaction gas is diluted by adjusting the nitrogen flow rate and the exhaust gas flow rate in advance. The downstream concentration can be kept low. Furthermore, by using the normally open solenoid valve 21, at the time of a power failure, the drive of the ejector 20 and the emergency exhaust line are automatically opened.
Exhaust can be performed without separately taking power outage countermeasures.

【0014】[0014]

【発明の効果】以上詳述したように本発明によれば、反
応容器からの排気と反応ガスの希釈を行うエゼクタを反
応容器と排気装置を結ぶラインに接続するように設け、
非常運転時にこのエゼクタを用いることにより、従来の
ように大型で高価な保守電源を用いることなく、反応容
器からの排気と反応ガスの希釈を行い、反応ガスを十分
に低い濃度で系外に放出できるとともに、反応容器の内
圧を大気圧以下に保持できる安全装置を提供できる。
As described above in detail, according to the present invention, an ejector for exhausting a reaction vessel and diluting a reaction gas is provided so as to be connected to a line connecting the reaction vessel and an exhaust device.
By using this ejector during an emergency operation, the reaction gas is exhausted from the reaction vessel and the reaction gas is diluted, and the reaction gas is discharged out of the system at a sufficiently low concentration without using a large and expensive maintenance power source as in the past. It is possible to provide a safety device capable of maintaining the internal pressure of the reaction vessel at or below the atmospheric pressure.

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

【図1】本発明の一実施例に係る安全装置の説明図。FIG. 1 is an explanatory view of a safety device according to one embodiment of the present invention.

【図2】従来の反応容器の排気装置の説明図。FIG. 2 is an explanatory view of a conventional exhaust device for a reaction vessel.

【符号の説明】[Explanation of symbols]

11…反応容器、 12…原料供給装置、 13…排気装置、 14…除害装置、 15…ベントスタック、 17…排気流量調節弁、 18…容器排気系閉鎖弁、 20…エゼクタ、 21…電磁弁、 22…窒素流量調節弁、 23…減圧弁、 25…窒素供給装置。 11 ... reaction vessel, 12 ... raw material supply device, 13 ... exhaust device, 14 ... abatement device, 15 ... vent stack, 17 ... exhaust flow rate control valve, 18 ... container exhaust system closing valve, 20 ... ejector, 21 ... solenoid valve , 22 ... nitrogen flow control valve, 23 ... pressure reducing valve, 25 ... nitrogen supply device.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 原料供給装置から原料及びプロセスガス
が供給され、内部で反応が行われる反応容器と、この反
応容器に接続され、該反応容器内部のガスを排気する排
気装置と、この排気装置に接続され、該排気装置内の排
気に含まれる有害成分を取り除く除害装置と、前記反応
容器と排気装置を結ぶラインに接続され、前記反応容器
からの排気とガスの希釈を行うエゼクタと、このエゼク
タに接続された窒素供給装置とを具備し、 通常運転時は、反応容器内を排気装置により排気し、除
外装置により有害ガスを取り除いた後排気し、 非常運転時は、窒素供給装置から窒素をエゼクタに供給
して、窒素の流動によりエゼクタの喉部に負圧を発生さ
せることにより、反応容器から反応ガスを排気すること
を特徴とする安全装置。
1. A reaction container in which a raw material and a process gas are supplied from a raw material supply device and a reaction is performed therein, an exhaust device connected to the reaction container and exhausting gas inside the reaction container, and an exhaust device Connected to a detoxification device that removes harmful components contained in the exhaust gas in the exhaust device, and an ejector that is connected to a line connecting the reaction container and the exhaust device and dilutes exhaust gas and gas from the reaction container, A nitrogen supply device connected to the ejector. During normal operation, the inside of the reaction vessel is evacuated by an exhaust device, and after removing harmful gases by an elimination device, the reaction container is evacuated. A safety device for supplying nitrogen to an ejector and generating a negative pressure in the throat of the ejector by the flow of nitrogen, thereby exhausting a reaction gas from a reaction vessel.
JP02048497A 1997-02-03 1997-02-03 Safety device Expired - Fee Related JP3801286B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP02048497A JP3801286B2 (en) 1997-02-03 1997-02-03 Safety device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP02048497A JP3801286B2 (en) 1997-02-03 1997-02-03 Safety device

Publications (2)

Publication Number Publication Date
JPH10220832A true JPH10220832A (en) 1998-08-21
JP3801286B2 JP3801286B2 (en) 2006-07-26

Family

ID=12028417

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5534158A (en) * 1978-09-01 1980-03-10 Sony Corp Vacuum reaction apparatus
JPS5740631A (en) * 1980-08-26 1982-03-06 Kansai Electric Power Co Inc:The Apparatus for diluting gas for measuring diameter of smoke dust grain
JPS6426832U (en) * 1987-08-07 1989-02-15
JPH05234986A (en) * 1992-02-20 1993-09-10 Mitsubishi Electric Corp Chemical vapor growing apparatus
JPH08172083A (en) * 1994-12-16 1996-07-02 Ebara Corp By-product trap device and cleaning thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5534158A (en) * 1978-09-01 1980-03-10 Sony Corp Vacuum reaction apparatus
JPS5740631A (en) * 1980-08-26 1982-03-06 Kansai Electric Power Co Inc:The Apparatus for diluting gas for measuring diameter of smoke dust grain
JPS6426832U (en) * 1987-08-07 1989-02-15
JPH05234986A (en) * 1992-02-20 1993-09-10 Mitsubishi Electric Corp Chemical vapor growing apparatus
JPH08172083A (en) * 1994-12-16 1996-07-02 Ebara Corp By-product trap device and cleaning thereof

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