JP2005214553A - Chemical agent-polluted area isolating method and its device - Google Patents

Chemical agent-polluted area isolating method and its device Download PDF

Info

Publication number
JP2005214553A
JP2005214553A JP2004024116A JP2004024116A JP2005214553A JP 2005214553 A JP2005214553 A JP 2005214553A JP 2004024116 A JP2004024116 A JP 2004024116A JP 2004024116 A JP2004024116 A JP 2004024116A JP 2005214553 A JP2005214553 A JP 2005214553A
Authority
JP
Japan
Prior art keywords
chemical agent
exhaust
contaminated
concentration
sealed structure
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
JP2004024116A
Other languages
Japanese (ja)
Other versions
JP4369767B2 (en
Inventor
Junpei Nakayama
準平 中山
Kiyoshi Asahina
潔 朝比奈
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.)
Kobe Steel Ltd
Original Assignee
Kobe Steel 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 Kobe Steel Ltd filed Critical Kobe Steel Ltd
Priority to JP2004024116A priority Critical patent/JP4369767B2/en
Publication of JP2005214553A publication Critical patent/JP2005214553A/en
Application granted granted Critical
Publication of JP4369767B2 publication Critical patent/JP4369767B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Abstract

<P>PROBLEM TO BE SOLVED: To provide a chemical agent-polluted area isolating method and its device capable of isolating an area polluted by a chemical agent and executing the work in safety inside of the isolated area. <P>SOLUTION: The chemical agent-polluted area is covered by a sealed construction 1, a plurality of exhaust ports 3 having a plurality of intake ports 2 and closure valves 6 are laterally arranged on opposite side walls 1a, 1b of the sealed construction 1, an activated charcoal filter 7 and a chemical agent detector 9 of a first stage, and an activated charcoal filter 8 and an exhauster 5 of a second stage are mounted at a downstream side of the plurality of exhaust ports 3. In a case when a concentration of chemical agent measured by the chemical agent detector 9 is over a permitted concentration, the exhauster 5 is stopped and the closure valves 6 are closed. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は、地中に遺棄された化学兵器を処理するために、化学剤で汚染された地域を外界から隔離する隔離技術に関する。   The present invention relates to an isolation technique for isolating an area contaminated with a chemical agent from the outside world in order to deal with chemical weapons abandoned in the ground.

地中に埋設して遺棄されている化学兵器や化学剤入りガラス瓶（以下、「化学兵器等」という。）の遺棄現場等で化学兵器等の探索作業、回収作業、安全化処理作業等（以下、「化学兵器等処理作業」と総称する。）を実施する場合、化学兵器等から化学剤が漏洩して一帯が汚染されていたり、化学兵器等処理作業に伴って新たに汚染が発生することが考えられる。このため、化学兵器等処理作業を行うに際し、作業現場をテント、建屋等の密閉構築物で覆った後、その内部を負圧にして、汚染物質が密閉構築物の外部に漏れ出さないようにしている（例えば、特許文献１参照）。   Exploration work, recovery work, safety treatment work, etc. of chemical weapons etc. (hereinafter referred to as “chemical weapons, etc.”) , "Collectively referred to as" chemical weapons processing operations "), chemical agents may leak from chemical weapons, etc., and the entire area may be contaminated, or new contamination will occur with chemical weapons processing operations. Can be considered. For this reason, when processing chemical weapons, etc., after covering the work site with a sealed structure such as a tent or building, the inside of the work is made negative pressure so that contaminants do not leak out of the sealed structure. (For example, refer to Patent Document 1).

化学兵器に用いられる化学剤は毒性物質であり、その多くは室温では液体あるいは固体であるが、揮発性を有し、かつ分子量が大きい（下記表１参照）。このため、汚染された箇所から化学剤の蒸気が連続的に放出されて密閉構築物の内部に充満し、特に地表面近傍に滞留しやすい。したがって、単に上記従来の方法で汚染地域を隔離すると外界に対しては安全であるが、密閉構築物の内部の作業環境はかえって悪化し、作業員に対して危険性が増大するおそれがある。


Figure 2005214553
特開２００２−１０７１００号公報 Chemical agents used in chemical weapons are toxic substances, many of which are liquid or solid at room temperature, but are volatile and have a high molecular weight (see Table 1 below). For this reason, the chemical agent vapor is continuously released from the contaminated portion, fills the inside of the sealed structure, and tends to stay particularly near the ground surface. Therefore, if the contaminated area is simply isolated by the conventional method described above, it is safe for the outside world, but the working environment inside the sealed structure is rather deteriorated, which may increase the danger to workers.


Figure 2005214553
 JP 2002-107100 A

そこで、本発明は、化学剤で汚染された地域（以下、「化学剤汚染地域」という。）を外界から隔離するとともに、その隔離された内部で安全に作業を実施することができる化学剤汚染地域の隔離方法およびその装置を提供することを目的とする。   Therefore, the present invention isolates an area contaminated with a chemical agent (hereinafter referred to as “chemical agent-contaminated area”) from the outside world, and allows chemical operations to be performed safely in the isolated interior. It is an object of the present invention to provide a local isolation method and apparatus.

請求項１に記載の発明は、化学剤で汚染された化学剤汚染地域を密閉構築物で覆い、この密閉構築物の内部を負圧に維持しつつ、当該密閉構築物の内部に一定方向の気流を形成するように換気を行うことを特徴とする化学剤汚染地域の隔離方法である。   According to the first aspect of the present invention, a chemical agent-contaminated area contaminated with a chemical agent is covered with a sealed structure, and an air flow in a certain direction is formed inside the sealed structure while maintaining the inside of the sealed structure at a negative pressure. This is a method for isolating a chemical agent-contaminated area characterized by performing ventilation.

請求項２に記載の発明は、請求項１に記載の方法において、前記換気による前記密閉構築物からの排気をろ過し、このろ過後の排気中の化学剤濃度を測定し、この化学剤濃度が許容濃度を超えた場合は、前記換気を中止するとともに、前記一定方向の気流が逆流することを防止する化学剤汚染地域の隔離方法である。   According to a second aspect of the present invention, in the method according to the first aspect, the exhaust from the sealed structure by the ventilation is filtered, and the chemical agent concentration in the exhaust gas after the filtration is measured. When the permissible concentration is exceeded, the ventilation is stopped and the chemical agent-contaminated area is isolated by preventing the airflow in the predetermined direction from flowing backward.

請求項３に記載の発明は、化学剤で汚染された化学剤汚染地域を覆う密閉構築物と、前記密閉構築物の一の側壁に横方向に並べて設けられた複数の入気口と、前記一の側壁に対向する側壁に横方向に並べて設けられた複数の排気口と、前記複数の排気口から排気を行う排風機とを備えたことを特徴とする化学剤汚染地域の隔離装置である。   According to a third aspect of the present invention, there is provided a sealed structure covering a chemical agent-contaminated area contaminated with a chemical agent, a plurality of air inlets provided side by side on one side wall of the sealed structure, and the one An isolation device for a chemical agent-contaminated area, comprising: a plurality of exhaust ports arranged side by side on a side wall opposite to the side walls; and a wind exhauster that exhausts air from the plurality of exhaust ports.

請求項４に記載の発明は、請求項３に記載の装置において、前記複数の入気口からの吸気を止める閉止弁と、前記複数の排気口からの排気をろ過する２段の活性炭フィルタと、この２段の活性炭フィルタの間に設けられ、前記排気中の化学剤濃度を測定する化学剤検知器とを備え、前記化学剤濃度が許容濃度を超えた場合は、前記排風機を停止するとともに、前記閉止弁を閉止するように構成された化学剤汚染地域の隔離装置である。   According to a fourth aspect of the present invention, in the apparatus according to the third aspect, a shut-off valve that stops intake from the plurality of inlets, a two-stage activated carbon filter that filters exhaust from the plurality of outlets, And a chemical agent detector provided between the two-stage activated carbon filters for measuring the chemical agent concentration in the exhaust, and when the chemical agent concentration exceeds an allowable concentration, the exhaust fan is stopped. And an isolation device for a chemical agent contaminated area configured to close the shut-off valve.

本発明によれば、密閉構築物の内部を負圧に維持しつつ、密閉構築物内に一定方向の気流を形成するように換気を行うことにより、汚染物質を外気中に漏らすことなく、かつ、揮発した化学剤の蒸気が密閉構築物の内部に滞留することを防止できる。したがって、化学剤汚染地域を外界から隔離するとともに、その隔離された内部で安全に作業を実施することが実現できる。   According to the present invention, while maintaining the inside of the closed structure at a negative pressure, ventilation is performed so as to form a certain direction of air flow in the closed structure, so that the contaminants are not leaked into the outside air and volatilized. It is possible to prevent the vapor of the chemical agent from staying inside the sealed structure. Therefore, it is possible to isolate the chemical agent-contaminated area from the outside world and safely perform the work inside the isolated area.

以下、本発明の実施形態について図面を参照しつつ詳細に説明する。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

図１および図２は、本発明の実施形態に係る化学剤汚染地域の隔離装置を示す概略説明図である。本例の隔離装置は、化学剤で汚染された化学剤汚染地域を覆う密閉構築物としての水平断面が矩形状のテント１と、このテント１の一の側壁１ａに横方向に並べて設けられた複数の入気口２と、側壁１ａに対向する側壁１ｂに横方向に並べて設けられた複数の排気口３と、これら複数の排気口３の下流側に枝管４ａを有する集合配管４を介して設けられ、これら複数の排気口３から排気を行う排風機５とを備えている。なお、入気口１および排気口２の径、設置数、設置間隔等は、テント１内に一定方向の気流が形成され、空気がよどむ部分ができないように、テント１の大きさ（幅、長さ、高さ等）、排風機５の能力等に応じて適宜調整すればよい。また、排気口２の設置高さは、地表面近傍に滞留しやすい化学剤蒸気を効率良く除去するため、可能な範囲で地表面に近付けて低くすることが望ましい。また、化学剤の中には比較的分子量が小さく、その蒸気が地表面から離れて上方に揮散するものも存在し得るので、入気口１の設置高さを地表面から離して高くしたり、入気口１および／または排気口２の設置高さを２種類以上として入気口１および／または排気口２を横方向に２列以上配置するようにしても良い。   FIG. 1 and FIG. 2 are schematic explanatory views showing a chemical agent contaminated area isolation device according to an embodiment of the present invention. The isolation device of this example includes a tent 1 having a rectangular horizontal cross section as a sealed structure covering a chemical agent-contaminated area contaminated with a chemical agent, and a plurality of side-by-side provided on one side wall 1a of the tent 1. Air inlet 2, a plurality of exhaust ports 3 provided side by side on the side wall 1 b facing the side wall 1 a, and a collecting pipe 4 having a branch pipe 4 a downstream of the plurality of exhaust ports 3. And an exhaust fan 5 that exhausts air from the plurality of exhaust ports 3. It should be noted that the diameter, the number of installations, and the installation interval of the air inlet 1 and the air outlet 2 are such that the airflow in a certain direction is formed in the tent 1 and the size of the tent 1 (width, Length, height, etc.), the capacity of the exhaust fan 5 and the like may be adjusted as appropriate. Further, the installation height of the exhaust port 2 is desirably as close to the ground surface as possible in order to efficiently remove chemical agent vapor that tends to stay near the ground surface. In addition, some chemical agents have a relatively low molecular weight, and the vapor of the chemical may volatilize upward away from the ground surface. Therefore, the installation height of the inlet 1 is increased away from the ground surface. Two or more kinds of installation heights of the air inlets 1 and / or the exhaust ports 2 may be provided, and two or more rows of the air inlets 1 and / or the exhaust ports 2 may be arranged in the horizontal direction.

排風機５を運転すると、排気口３からテント１内の空気が吸引排気されてテント１内が負圧となり、これにともない入気口２から外気がテント１内に吸引される。ここで、入気口２と排気口３とを対向する側壁に横方向に並べて複数個ずつ配しているので、テント１内において入気口２から排気口３へと向かう一定方向の空気の流れ（気流）が形成される（図３参照；図３は、市販の流体解析ソフトウェア［ＦＬＵＥＮＴ ６．０（商品名）］を用いて、矩形水平断面を有するテント１の短辺側の対向する側壁１ａ，１ｂのそれぞれに８個の入気口２と６個の排気口３を水平方向に並べて設けた場合にテント１内の地表面近傍に生じる気流の流速分布を計算により求めたものである。なお、流速分布はテント１の長手方向に向かって左右対象であるので、テント１の幅の１／２の部分のみを示した。）。これにより、揮発した化学剤の蒸気Ｂは前記気流によって常に風下に向かって押し流され、排気口３から吸引排気されるため、化学剤蒸気Ｂがテント内１に滞留することがない。また、処理対象物Ａの風上側から作業することより、処理対象物Ａから発生する高濃度の化学剤蒸気Ｂに直接曝されることが防止されるので、作業員Ｃの安全をより確実に確保することができる。   When the exhaust fan 5 is operated, the air in the tent 1 is sucked and exhausted from the exhaust port 3, and the inside of the tent 1 becomes negative pressure. As a result, outside air is sucked into the tent 1 from the air inlet 2. Here, since the air inlet 2 and the air outlet 3 are arranged side by side on the opposite side wall in a lateral direction, a plurality of air in a certain direction from the air inlet 2 to the air outlet 3 in the tent 1 are arranged. A flow (airflow) is formed (see FIG. 3; FIG. 3 shows the opposite side of the short side of the tent 1 having a rectangular horizontal cross section using commercially available fluid analysis software [FLUENT 6.0 (trade name)]. The flow velocity distribution of airflow generated near the ground surface in the tent 1 when 8 inlets 2 and 6 exhausts 3 are arranged in the horizontal direction in each of the side walls 1a and 1b is obtained by calculation. In addition, since the flow velocity distribution is an object on the left and right sides in the longitudinal direction of the tent 1, only a half portion of the width of the tent 1 is shown. As a result, the vapor B of the chemical agent that has volatilized is always pushed down toward the lee by the air flow and is sucked and exhausted from the exhaust port 3, so that the chemical agent vapor B does not stay in the tent 1. In addition, since working from the windward side of the processing object A is prevented from being directly exposed to the high-concentration chemical agent vapor B generated from the processing object A, the safety of the worker C is more reliably ensured. Can be secured.

上記隔離装置は、さらに、複数の入気口２からの吸気を止めるために各入気口２に設けられた閉止弁６と、複数の排気口３からの排気をろ過する２段の活性炭フィルタ７，８と、この２段の活性炭フィルタ７，８の間に設けられ、前記排気中の化学剤濃度を測定する化学剤検知器９とを備え、前記化学剤濃度が許容濃度を超えた場合は、排風機５を停止するとともに、閉止弁６を閉止するように構成するのが好ましい。つまり、排気口３から排出された排気は１段目の活性炭フィルタ７でろ過され、排気中の化学剤蒸気が吸着除去される。１段目の活性炭フィルタ７でろ過された後の排気中に残存する化学剤の濃度は、化学剤検知器９で連続的または間欠的に測定される。そして、化学剤検知器９で測定された化学剤濃度が所定の許容濃度以下である場合は、この排気は２段目の活性炭フィルタ８でさらにろ過され化学剤濃度は一層低下するので、そのまま外気中に放出することができる。一方、活性炭フィルタ７のろ過能力（吸着能力）の劣化等により前記化学剤濃度が所定の許容濃度を超えた場合は、排風機５を停止することにより、高濃度の化学剤を含有する排気が外気中に放出されることを防止する。ここで、化学剤濃度が所定の許容濃度を超えたことを検知したときには、すでに排気は外気外に放出されているが、検知位置より下流側にも活性炭フィルタ８が備えられているので、この排気は２段目の活性炭フィルタ８でろ過されて化学剤濃度が許容濃度以下に低下するため、安全に外気中に放出できる。また、排風機５を停止すると、テント１内の化学剤蒸気を含有する気流が逆流して入気口２から外気に放出されるおそれがあるが、入気口２に設けられた閉止弁６を閉止することにより、これを防止することができる。なお、排風機５を停止するとともに閉止弁６を閉止すると、やがてテント１内は外気と同圧となり、テント１に設けられた作業員が出入りするためのドアの隙間などごく限られた隙間から化学剤が外気中に拡散し始めるが、このような隙間からの拡散による漏洩速度は非常に緩やかであるため、テント１から一定の距離以上離れた場所では外気中の化学剤濃度は十分に低下しており安全が維持される。   The isolation device further includes a shutoff valve 6 provided in each inlet 2 to stop intake from the plurality of inlets 2 and a two-stage activated carbon filter that filters exhaust from the plurality of outlets 3. 7 and 8 and a chemical agent detector 9 provided between the two-stage activated carbon filters 7 and 8 for measuring the chemical agent concentration in the exhaust gas, and the chemical agent concentration exceeds an allowable concentration. Is preferably configured to stop the exhaust fan 5 and to close the closing valve 6. That is, the exhaust gas discharged from the exhaust port 3 is filtered by the first-stage activated carbon filter 7, and the chemical agent vapor in the exhaust gas is adsorbed and removed. The concentration of the chemical agent remaining in the exhaust gas after being filtered by the first-stage activated carbon filter 7 is continuously or intermittently measured by the chemical agent detector 9. If the chemical agent concentration measured by the chemical agent detector 9 is below a predetermined allowable concentration, the exhaust gas is further filtered by the second stage activated carbon filter 8 and the chemical agent concentration is further reduced. Can be released inside. On the other hand, when the chemical agent concentration exceeds a predetermined allowable concentration due to deterioration of the filtration capability (adsorption capability) of the activated carbon filter 7 or the like, the exhaust gas containing the high concentration chemical agent is removed by stopping the exhaust fan 5. Prevent from being released into the open air. Here, when it is detected that the chemical agent concentration exceeds a predetermined allowable concentration, the exhaust gas has already been released to the outside of the atmosphere, but the activated carbon filter 8 is also provided on the downstream side from the detection position. The exhaust gas is filtered through the second-stage activated carbon filter 8 and the chemical agent concentration falls below the allowable concentration, so that it can be safely discharged into the outside air. Further, when the exhaust fan 5 is stopped, the air flow containing the chemical agent vapor in the tent 1 may flow backward and be released to the outside air from the inlet 2, but the closing valve 6 provided at the inlet 2. This can be prevented by closing. When the exhaust fan 5 is stopped and the shut-off valve 6 is closed, the tent 1 eventually becomes the same pressure as the outside air, and from a limited space such as a door clearance for an operator provided in the tent 1 to enter and exit. The chemical agent begins to diffuse into the outside air, but the leakage rate due to diffusion through such a gap is very slow, so the concentration of the chemical agent in the outside air is sufficiently reduced at a distance of a certain distance from the tent 1. Safety is maintained.

また、図２に示すように、集合配管４の下流側を２つの系統に分岐して、各系統にそれぞれ２段の活性炭フィルタ７，８および排風機５を設け、化学剤検知器９は両系統兼用としておくことが好ましい。これにより、例えば、一方の系統をオンラインとし、他方の系統をスタンバイとして用い、オンラインの系統でフィルタ７，８のろ過（吸着）能力の低下、配管詰まり、排風機６の故障等のトラブルが発生した場合は、スタンバイの系統をオンラインに切り替えて換気性能を維持しつつ、その間にトラブルの発生した側の系統のメンテナンスを行うことができる。   In addition, as shown in FIG. 2, the downstream side of the collecting pipe 4 is branched into two systems, and each system is provided with two stages of activated carbon filters 7 and 8 and an exhaust fan 5, respectively. It is preferable to share the system. As a result, for example, one of the systems is set online and the other system is used as a standby system. Problems such as a decrease in the filtration (adsorption) capacity of the filters 7 and 8 in the online system, clogging of the pipes, failure of the exhaust fan 6 occur. In this case, the standby system can be switched to online to maintain the ventilation performance, while the system on the trouble side can be maintained during that time.

（変形例）
上記実施形態では、密閉構築物１としてテントを例示したが、建屋としても良い。また、閉止弁６は複数の入気口２のそれぞれに設けた例を示したが、複数の入気口２の上流側にそれぞれダクトを取り付け、これらのダクトを集合した集合ダクトに１つの閉止弁６を設けるようにしても良い。また、集合配管４の下流側の２系統のうち、一方をオンライン、他方をスタンバイとする例を示したが、両系統ともオンラインとし、一方の系統にトラブルが発生した時には他方のみを運転し、その間に前記一方の系統のメンテナンスを行うようにしても良い。また、化学剤検知器９は両系統兼用とした例を示したが、両系統にそれぞれ設けても良い。また、排風機５は両系統それぞれに設けた例を示したが、両系統兼用としても良い。 (Modification)
In the said embodiment, although the tent was illustrated as the sealed structure 1, it is good also as a building. Moreover, although the example which provided the shut-off valve 6 in each of several inlets 2 was shown, it attaches a duct to the upstream of the several inlets 2, respectively, and closes one closing to the collective duct which collected these ducts. A valve 6 may be provided. In addition, although an example in which one of the two systems on the downstream side of the collective piping 4 is online and the other is a standby is shown, both systems are online, and when a trouble occurs in one system, only the other is operated. In the meantime, the maintenance of the one system may be performed. Moreover, although the chemical agent detector 9 showed the example which used both systems, you may provide in both systems, respectively. Moreover, although the example which provided the exhaust fan 5 in each of both systems was shown, it is good also as both systems combined use.

実施形態に係る化学剤汚染地域の隔離装置の概略を示す縦断面図である。It is a longitudinal cross-sectional view which shows the outline of the isolation apparatus of the chemical agent contamination area which concerns on embodiment. 実施形態に係る化学剤汚染地域の隔離装置の概略を示す平面図である。It is a top view which shows the outline of the isolation apparatus of the chemical agent contamination area which concerns on embodiment. テント内の地表面近傍に生じる気流の流速分布を示す等流速線図である。It is an equal velocity diagram which shows the flow velocity distribution of the airflow produced in the ground surface vicinity in a tent.

符号の説明Explanation of symbols

１：密閉構築物（テント）
１ａ，１ｂ：側壁
２：入気口
３：排気口
４：集合配管
４ａ：枝管
５：排風機
６：閉止弁
７，８：活性炭フィルタ
９：化学剤検知器
Ａ：処理対象物
Ｂ：化学剤蒸気
Ｃ：作業員

1: Sealed structure (tent)
DESCRIPTION OF SYMBOLS 1a, 1b: Side wall 2: Inlet port 3: Exhaust port 4: Collective piping 4a: Branch pipe 5: Exhaust pipe 6: Shut-off valve 7, 8: Activated carbon filter 9: Chemical agent detector A: Process target B: Chemical Chemical vapor C: Worker

Claims (4)

化学剤で汚染された化学剤汚染地域を密閉構築物で覆い、この密閉構築物の内部を負圧に維持しつつ、当該密閉構築物の内部に一定方向の気流を形成するように換気を行うことを特徴とする化学剤汚染地域の隔離方法。   Covering a chemical agent-contaminated area contaminated with a chemical agent with a sealed structure, and maintaining the inside of the sealed structure at a negative pressure while ventilating to form an air flow in a certain direction inside the sealed structure. The isolation method of the chemical agent contamination area. 請求項１に記載の方法において、前記換気による前記密閉構築物からの排気をろ過し、このろ過後の排気中の化学剤濃度を測定し、この化学剤濃度が許容濃度を超えた場合は、前記換気を中止するとともに、前記一定方向の気流が逆流することを防止する化学剤汚染地域の隔離方法。   The method according to claim 1, wherein the exhaust from the closed structure by the ventilation is filtered, the chemical agent concentration in the exhaust after the filtration is measured, and if the chemical agent concentration exceeds an allowable concentration, A method for isolating a chemical agent-contaminated region that stops ventilation and prevents the airflow in a certain direction from flowing backward. 化学剤で汚染された化学剤汚染地域を覆う密閉構築物と、前記密閉構築物の一の側壁に横方向に並べて設けられた複数の入気口と、前記一の側壁に対向する側壁に横方向に並べて設けられた複数の排気口と、前記複数の排気口から排気を行う排風機とを備えたことを特徴とする化学剤汚染地域の隔離装置。   A sealed structure covering a chemical agent-contaminated area contaminated with a chemical agent, a plurality of air inlets arranged side by side on one side wall of the sealed structure, and a side wall facing the one side wall in a lateral direction An isolation device for a chemical agent-contaminated area, comprising: a plurality of exhaust ports arranged side by side; and a wind exhauster that exhausts air from the plurality of exhaust ports. 請求項３に記載の装置において、前記複数の入気口からの吸気を止める閉止弁と、前記複数の排気口からの排気をろ過する２段の活性炭フィルタと、この２段の活性炭フィルタの間に設けられ、前記排気中の化学剤濃度を測定する化学剤検知器とを備え、前記化学剤濃度が許容濃度を超えた場合は、前記排風機を停止するとともに、前記閉止弁を閉止するように構成された化学剤汚染地域の隔離装置。

4. The apparatus according to claim 3, wherein a shut-off valve that stops intake from the plurality of inlets, a two-stage activated carbon filter that filters the exhaust from the plurality of outlets, and the two-stage activated carbon filter are provided. And a chemical agent detector for measuring the chemical agent concentration in the exhaust gas. When the chemical agent concentration exceeds an allowable concentration, the exhaust fan is stopped and the shutoff valve is closed. Contained equipment for chemical agent contaminated areas.

JP2004024116A 2004-01-30 2004-01-30 Method and apparatus for isolating chemical agent contaminated area Expired - Fee Related JP4369767B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2004024116A JP4369767B2 (en) 2004-01-30 2004-01-30 Method and apparatus for isolating chemical agent contaminated area

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2004024116A JP4369767B2 (en) 2004-01-30 2004-01-30 Method and apparatus for isolating chemical agent contaminated area

Publications (2)

Publication Number Publication Date
JP2005214553A true JP2005214553A (en) 2005-08-11
JP4369767B2 JP4369767B2 (en) 2009-11-25

Family

ID=34906901

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2004024116A Expired - Fee Related JP4369767B2 (en) 2004-01-30 2004-01-30 Method and apparatus for isolating chemical agent contaminated area

Country Status (1)

Country Link
JP (1) JP4369767B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007132634A1 (en) * 2006-05-11 2007-11-22 Kabushiki Kaisha Kobe Seiko Sho Blasting processing device
WO2007132614A1 (en) * 2006-05-16 2007-11-22 Kabushiki Kaisha Kobe Seiko Sho Explosion treatment system and explosion treatment method
JP2013226428A (en) * 2006-08-16 2013-11-07 Rescue Air Systems Inc Safety system for breathable air distribution, and method and building structure thereof

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007132634A1 (en) * 2006-05-11 2007-11-22 Kabushiki Kaisha Kobe Seiko Sho Blasting processing device
US7866244B2 (en) 2006-05-11 2011-01-11 Kobe Steel, Ltd. Blasting treatment apparatus
WO2007132614A1 (en) * 2006-05-16 2007-11-22 Kabushiki Kaisha Kobe Seiko Sho Explosion treatment system and explosion treatment method
JP2007309550A (en) * 2006-05-16 2007-11-29 Kobe Steel Ltd Treatment system and treatment method
JP4667301B2 (en) * 2006-05-16 2011-04-13 株式会社神戸製鋼所 Processing system and processing method
US8153855B2 (en) 2006-05-16 2012-04-10 Kobe Steel, Ltd. Blasting system and blasting method
JP2013226428A (en) * 2006-08-16 2013-11-07 Rescue Air Systems Inc Safety system for breathable air distribution, and method and building structure thereof

Also Published As

Publication number Publication date
JP4369767B2 (en) 2009-11-25

Similar Documents

Publication Publication Date Title
CN101457961B (en) Air filtration for nuclear reactor habitability area
CN101457960A (en) Air filtration and handling for nuclear reactor habitability area
JPH0480538A (en) Air conditioner for clean room
JP4369767B2 (en) Method and apparatus for isolating chemical agent contaminated area
KR101929696B1 (en) Ion implanter comprising integrated ventilation system
KR20180114259A (en) Safety Cabinet
JPH08219511A (en) Small environment for dangerous manufacture tool
CN203090632U (en) Efficient leak detection and gas disinfection type high-efficiency air filtering device
KR102209052B1 (en) Gas flushing apparatus
KR20180132025A (en) Biological Safety Cabinet
JP3701209B2 (en) Reactor ventilation equipment
KR102240826B1 (en) Auto Ventilation System for Subway
JPH0647269A (en) Vacuum treating device
JP5780065B2 (en) Shelter emergency ventilator intake / exhaust piping connection penetration unit and assembly connection method
KR20170044227A (en) A Filtering Apparatus for an Intake Air of a System of Air Management
JP7390084B1 (en) Air purification equipment and air purification systems
JP6006952B2 (en) Cesium removal treatment equipment
JP2000346984A (en) Purification system for atmosphere in condenser
CN213378467U (en) Physical ventilation system for repairing soil VOCs pollution
KR20190112547A (en) Ventilation system for internal cleaning of pipes
Gherghe et al. SPECIFIC OPERATING CONDITIONS AND TYPE-DIMENSIONS OF INDUSTRIAL VENTILATION SYSTEMS
KR20160141977A (en) Ventilator and Leakage Comprobador for preventing a outside leakage of harmful dangerous substance in local area
EP2865424A1 (en) Air compressor system
JP2006266624A (en) Exhaust device for safety cabinet
KR200362528Y1 (en) apparatus for smoke-proof

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060925

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20081224

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20081225

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090220

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20090609

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20090807

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20090825

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20090828

R150 Certificate of patent or registration of utility model

Ref document number: 4369767

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120904

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120904

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130904

Year of fee payment: 4

LAPS Cancellation because of no payment of annual fees