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JP3801286B2 - Safety device - Google Patents
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JP3801286B2 - Safety device - Google Patents

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Publication number
JP3801286B2
JP3801286B2 JP02048497A JP2048497A JP3801286B2 JP 3801286 B2 JP3801286 B2 JP 3801286B2 JP 02048497 A JP02048497 A JP 02048497A JP 2048497 A JP2048497 A JP 2048497A JP 3801286 B2 JP3801286 B2 JP 3801286B2
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Japan
Prior art keywords
reaction vessel
exhaust
ejector
nitrogen
gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
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JP02048497A
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Japanese (ja)
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JPH10220832A (en
Inventor
健一郎 小阪
康弘 山内
明人 小森
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Mitsubishi Heavy Industries Ltd
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Mitsubishi Heavy Industries Ltd
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Priority to JP02048497A priority Critical patent/JP3801286B2/en
Publication of JPH10220832A publication Critical patent/JPH10220832A/en
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Description

【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。
【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。
【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。
【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。
【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。
【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、前記エゼクタと窒素供給装置を結ぶラインに介装された、ノーマルオープンの電磁弁とを具備し、通常運転時は、反応容器内を排気装置により排気し、除害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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【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。
【図面の簡単な説明】
【図1】本発明の一実施例に係る安全装置の説明図。
【図2】従来の反応容器の排気装置の説明図。
【符号の説明】
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。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a safety device, and more particularly to a safety device used for an exhaust facility at the time of emergency stop of a facility that uses harmful gas or high-temperature gas.
[0002]
[Prior art]
Conventionally, the example shown in FIG. 2 is known as an example of an exhaust device for a reaction vessel.
Number 1 in the figure is a reaction vessel. The reaction vessel 1 is connected to a raw material supply device 2 for supplying raw materials and process gas to the reaction vessel 1, and a reaction is performed in the reaction vessel 1. The raw material supply device 2 is configured to automatically stop the supply of raw materials 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 the reaction product and the process gas in the reaction vessel 1 contain harmful components, the exhaust device 3 exhausts the internal gas, and the removal device 4 removes the harmful components contained in the exhaust. Then, it is discharged from the vent stack 5 to the atmosphere. Here, the exhaust device 3 has a function of exhausting the inside of the reaction vessel 1 and keeping the inside of the reaction vessel 1 at atmospheric pressure or lower to prevent leakage from the reaction vessel 1 to the outside.
[0003]
A line connecting the reaction vessel 1 and the exhaust device 3 and a line connecting the detoxifying device 4 and the vent stack 5 are connected by a line 8 having a pre-exhaust device 6 and a pre-detoxifying device 7 interposed therebetween. The preliminary exhaust device 6 and the preliminary abatement device 7 are installed for backup when the exhaust device 3 and the abatement device 4 fail. A safety power source 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]
[Problems to be solved by the invention]
However, in the conventional reaction vessel exhaust device, the safety power source 9 such as an uninterruptible power source for driving the exhaust device 3, the abatement device 4, the preliminary exhaust device 6, and the preliminary abatement device 7 is large and expensive. In addition, maintenance and inspection are required. In addition, a backup is necessary to ensure the reliability of the abatement device including the mechanical drive unit and the exhaust device.
[0005]
The present invention has been made in consideration of such circumstances, and an ejector for exhausting the reaction vessel and diluting the reaction gas is provided so as to be connected to a line connecting the reaction vessel and the exhaust device, and this ejector is used during an emergency operation. Therefore, without using a large and expensive maintenance power source as in the past, the reaction vessel can be exhausted and the reaction gas diluted, and the reaction gas can be released out of the system at a sufficiently low concentration. An object of the present invention is to provide a safety device that can keep the pressure below atmospheric pressure.
[0006]
[Means for Solving the Problems]
The present invention provides a reaction vessel in which a raw material and a process gas are supplied from a raw material supply device and a reaction is performed inside, an exhaust device connected to the reaction vessel and exhausting the gas inside the reaction vessel, and the exhaust device A detoxification device connected to remove harmful components contained in the exhaust gas in the exhaust device, an ejector connected to a line connecting the reaction vessel and the exhaust device, and for diluting the exhaust gas from the reaction vessel and the gas; A nitrogen supply device connected to the ejector, and a normally open solenoid valve interposed in a line connecting the ejector and the nitrogen supply device, and during normal operation, the reaction vessel is evacuated by an exhaust device, evacuated after removing harmful gases by scrubbing apparatus, emergency operation, the nitrogen from nitrogen supply device is supplied to the ejector to generate a negative pressure in the throat of the ejector by the flow of nitrogen More, a safety device, characterized by evacuating the reaction gas from the reaction vessel.
[0007]
(Function)
i) A nitrogen supply device using a liquid nitrogen tank can stably supply nitrogen gas without using power, and can exhaust and dilute the reaction gas even during a power failure.
[0008]
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 atmospheric pressure or lower without electric power.
iii) 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]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, a safety device according to an embodiment of the present invention will be described with reference to FIG.
Reference numeral 11 in the figure is a reaction vessel. The reaction vessel 11 is connected to a raw material supply device 12 for supplying raw materials and process gas to the reaction vessel 11, and the reaction is performed in the reaction vessel 11. In the raw material supply device 12, the supply of the raw material is automatically stopped in an emergency by an interlock device. Exhaust equipment such as an exhaust device 13, an abatement device 14, and a vent stack 15 are sequentially connected to the reaction vessel 11.
[0010]
An ejector 20 is connected to a line 16 connecting the reaction vessel 11 and the exhaust device 13 via a line 19 in which an exhaust flow rate control valve 17 and a vessel exhaust system closing valve 18 are sequentially provided. Here, the exhaust flow rate adjusting 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 having a normally open solenoid valve 21, a nitrogen flow rate adjustment valve 22, and a pressure reducing valve 23 in order from the ejector 20 side. Here, the nitrogen flow rate adjusting valve 22 adjusts the nitrogen flow rate, and the pressure reducing valve 23 adjusts the nitrogen pressure. In addition, the solenoid valve 21 is closed during normal operation and opened in an emergency.
[0011]
As described above, the safety device according to the embodiment includes the reaction vessel 11 connected to the raw material supply device 12, the exhaust device 13, the detoxification device 14 and the vent stack 15 sequentially connected to the reaction vessel 11. Exhaust flow rate control valve 17 connected to line 16 connecting reaction vessel 11 and exhaust device 13, vessel exhaust system closing valve 18 and ejector 20, electromagnetic valve 21 connected to this ejector 20, nitrogen flow rate control valve 22, decompression The valve 23 and the nitrogen supply device 25 are provided. The operation of the safety device having such a configuration during an ordinary operation or an emergency such as a power failure is as follows.
[0012]
i) During normal operation: The reaction vessel 11 is evacuated by the exhaust device 13, the harmful gas is removed by using the abatement device 14, and then exhausted by the vent stack 15.
ii) Emergency: The raw material supply device 12 is automatically stopped by the interlock device. Since the solenoid valve 21 is normally open, it is automatically opened in an emergency. When the electromagnetic 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 rate adjusting valve 22, and the electromagnetic valve 21. A negative pressure is generated in the throat of the ejector 20 due to the flow of 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 preliminarily adjusted using the pressure reducing valve 23, the flow rate of nitrogen is controlled by the nitrogen flow rate adjusting valve 22, and the exhaust flow rate from the reaction vessel 11 is previously set using the exhaust flow rate adjusting valve 17. Adjust it. The container exhaust system closing valve 18 is a normally open solenoid valve 21 that is closed during normal operation, and closes the line to the ejector 20, but is opened in an emergency and opens the exhaust line to the ejector 20. To do.
[0013]
The safety device according to the embodiment has the effects described below. First, if the nitrogen flow rate is ensured, the ejector 20 generates negative pressure in the throat and can suck out the reaction gas from the reaction vessel 11. Further, when driving the ejector 20, since the driving nitrogen is supplied from the nitrogen supply device 25 to the ejector 20, the reaction gas is diluted by adjusting the flow rate of nitrogen and the flow rate of exhaust gas in advance. The downstream concentration can be kept low. Furthermore, by using the normally open solenoid valve 21, the drive of the ejector 20 and the emergency exhaust line are automatically opened in the event of a power failure, so that exhaust can be performed without taking measures against power failure separately. .
[0014]
【The invention's effect】
As described above in detail, according to the present invention, an ejector for exhausting the reaction vessel and diluting the reaction gas is provided so as to be connected to a line connecting the reaction vessel and the exhaust device, and this ejector is used during emergency operation. Without using a large and expensive maintenance power supply as in the past, exhausting the reaction vessel and diluting the reaction gas can discharge the reaction gas outside the system at a sufficiently low concentration, while increasing the internal pressure of the reaction vessel. It is possible to provide a safety device that can be maintained below atmospheric pressure.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram of a safety device according to an embodiment of the present invention.
FIG. 2 is an explanatory view of a conventional exhaust device for a reaction vessel.
[Explanation of symbols]
11 ... reaction vessel,
12 ... Raw material supply equipment,
13 ... exhaust system,
14 ... abatement equipment,
15 ... Vent stack,
17… Exhaust flow control valve,
18 ... Vessel exhaust system closing valve,
20 ... Ejecta,
21 ... Solenoid valve,
22… Nitrogen flow control valve,
23 ... pressure reducing valve,
25 ... Nitrogen supply device.

Claims (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、前記エゼクタと窒素供給装置を結ぶラインに介装された、ノーマルオープンの電磁弁とを具備し、
通常運転時は、反応容器内を排気装置により排気し、除害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。
A raw material and a process gas are supplied from a raw material supply device, and a reaction vessel in which a reaction is performed is connected, an exhaust device connected to the reaction vessel and exhausting the gas inside the reaction vessel, connected to the exhaust device, and An abatement device that removes harmful components contained in the exhaust gas in the exhaust device, an ejector that is connected to the line connecting the reaction vessel and the exhaust device, and that performs exhaust and gas dilution from the reaction vessel, and is connected to this ejector A nitrogen supply device, and a normally open solenoid valve interposed in a line connecting the ejector and the nitrogen supply device ,
During normal operation, the reaction vessel is evacuated with an exhaust device, exhausted after removing harmful gases with an abatement device,
A safety device characterized in that during emergency operation, nitrogen is supplied from a nitrogen supply device to the ejector and a negative pressure is generated in the throat of the ejector by the flow of nitrogen, thereby exhausting the reaction gas from the reaction vessel.
JP02048497A 1997-02-03 1997-02-03 Safety device Expired - Fee Related JP3801286B2 (en)

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JP3801286B2 true JP3801286B2 (en) 2006-07-26

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JPH0729626Y2 (en) * 1987-08-07 1995-07-05 ソニー株式会社 Reduced pressure gas phase treatment equipment
JP3098093B2 (en) * 1992-02-20 2000-10-10 三菱電機株式会社 Chemical vapor deposition equipment
JP3539446B2 (en) * 1994-12-16 2004-07-07 株式会社荏原製作所 By-product trap device and cleaning method thereof

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