JP2960012B2 - Decompression device for gas fire extinguishing equipment - Google Patents

Decompression device for gas fire extinguishing equipment

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Publication number
JP2960012B2
JP2960012B2 JP16113796A JP16113796A JP2960012B2 JP 2960012 B2 JP2960012 B2 JP 2960012B2 JP 16113796 A JP16113796 A JP 16113796A JP 16113796 A JP16113796 A JP 16113796A JP 2960012 B2 JP2960012 B2 JP 2960012B2
Authority
JP
Japan
Prior art keywords
gas
fire extinguishing
pressure
flow path
fire
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 - Lifetime
Application number
JP16113796A
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Japanese (ja)
Other versions
JPH09319439A (en
Inventor
明人 岡本
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.)
KOOATSU KK
Original Assignee
KOOATSU KK
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Priority to JP16113796A priority Critical patent/JP2960012B2/en
Publication of JPH09319439A publication Critical patent/JPH09319439A/en
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Publication of JP2960012B2 publication Critical patent/JP2960012B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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、消火剤ガス貯蔵容
器内にガス状態で貯蔵されている不活性消火剤ガスを消
火対象区画内に放出し、消火対象区画内の消火剤の濃度
を消炎濃度以上に維持することによって消火するように
したガス系消火設備において、高圧の供給側ガス圧を所
定の出口側ガス圧に減圧するために用いられるガス系消
火設備用減圧装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a fire extinguishing agent gas storage container, which discharges an inert fire extinguishing agent gas stored in a gaseous state into a fire extinguishing target compartment and extinguishes the concentration of the fire extinguishing agent in the fire extinguishing target compartment. BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure reducing device for a gas fire extinguishing system, which is used to extinguish a fire by maintaining the concentration at or higher than the concentration, so as to reduce a high-pressure supply gas pressure to a predetermined outlet gas pressure.

【0002】[0002]

【従来の技術】従来、消火対象区画内に消火剤を放出
し、消火対象区画内の消火剤の濃度を消炎濃度以上に維
持することによって消火するようにしたガス系消火設備
として、消火剤に二酸化炭素やハロンガス等の不活性ガ
スを使用するようにしたものが実用化されている。
2. Description of the Related Art Conventionally, a fire extinguisher has been used as a gas fire extinguishing system in which a fire extinguishing agent is discharged into a fire extinguishing section and the fire extinguishing agent is extinguished by maintaining the concentration of the fire extinguishing agent in the fire extinguishing section higher than the flame-extinguishing concentration. Those using an inert gas such as carbon dioxide or halon gas have been put to practical use.

【0003】ところで、消火剤として二酸化炭素やハロ
ンガス等の不活性ガスを使用する場合、これらの消火剤
を加圧液化して高圧ガス容器からなる消火剤ガス貯蔵容
器に充填された状態で消火設備内に保管しておき、火災
の際に、適宜の電気的手段又は空圧的手段を用いて、消
火剤ガス貯蔵容器の容器弁を開放することにより、二酸
化炭素やハロンガスを消火剤ガス貯蔵容器から配管を介
して噴射ヘッドまで送り、噴射ヘッドから消火対象区画
内に放出するようにしている。このとき、二酸化炭素や
ハロンガス等の不活性ガスは、噴射ヘッドまでは液体の
状態で送られ、噴射ヘッドから消火対象区画内に放出さ
れた瞬間に気化して気体の状態となり、消火対象区画内
に充満して火災を鎮圧する。
When an inert gas such as carbon dioxide or halon gas is used as a fire extinguishing agent, these extinguishants are pressurized and liquefied and filled in a fire extinguisher gas storage container composed of a high-pressure gas container to extinguish fire extinguishing equipment. In the event of a fire, use appropriate electrical or pneumatic means to open the container valve of the fire extinguishing agent gas storage container to remove carbon dioxide and halon gas from the fire extinguishing agent gas storage container. From the nozzle to the injection head via a pipe, and discharges from the injection head into the fire extinguishing target compartment. At this time, the inert gas such as carbon dioxide and halon gas is sent in a liquid state to the ejection head, and is vaporized at the moment when the gas is released from the ejection head into the fire extinguishing section, and becomes a gaseous state. To suppress the fire.

【0004】そして、これらの二酸化炭素やハロンガス
等の不活性ガスを使用するガス系消火設備は、急速に火
災を鎮圧できること、消火剤による消火対象区画内の汚
染がほとんどないこと、電気の絶縁性を損なわないこ
と、消火剤が隙間から浸透して構造が複雑な消火対象に
対しても強力な消火効果を発揮できること、消火剤の経
年変化がなく長期に亘って一定の消火能力を有すること
等の利点を有することから、石油関連施設、電気関連施
設のみならず、一般の施設にも広く使用されている。
A gas fire extinguishing system using an inert gas such as carbon dioxide or halon gas is capable of rapidly suppressing a fire, hardly contaminating a fire extinguishing agent with a fire extinguishing agent, and having an electrical insulating property. That the fire extinguishing agent can penetrate through gaps and exert a strong fire-extinguishing effect even on fire-extinguishing objects with a complicated structure, and that the fire extinguishing agent has a constant fire-extinguishing ability over a long period without aging. It is widely used not only in petroleum-related facilities and electrical facilities, but also in general facilities.

【0005】ところが、近年になって、オゾン層の破壊
に関する問題が世界的な規模で提起され、ハロンガス等
のハロゲン化炭化水素成分を含有する消火剤について
は、1994年1月に生産中止となり、事実上使用する
ことができなくなった。これにより、アルゴン等の高価
な希ガスを使用する特殊な消火設備を除くと、現在、ガ
ス系消火設備において使用されている消火剤は、二酸化
炭素のみであるということができる。
However, in recent years, a problem relating to destruction of the ozone layer has been raised on a worldwide scale, and production of fire extinguishing agents containing halogenated hydrocarbon components such as halon gas was discontinued in January 1994. It is virtually unusable. Accordingly, excluding special fire extinguishing equipment using expensive rare gas such as argon, it can be said that the fire extinguishing agent currently used in gas fire extinguishing equipment is only carbon dioxide.

【0006】一方、この二酸化炭素を消火剤として使用
する消火設備についても、以下の問題点があることが知
られている。 (1) 消火時の消火対象区画内の二酸化炭素の設計濃度
は、約35%であり、この濃度では、万一消火対象区画
内に人が存在していた場合、二酸化炭素の毒性(麻酔
性)により人命に係わる事態が発生するおそれがある。 (2) 二酸化炭素は、火災の際、噴射ヘッドまでは液体の
状態で送られ、噴射ヘッドから消火対象区画内に放出さ
れた瞬間に気化して気体の状態となるが、このとき、周
囲から気化熱を奪うため室内の空気の飽和蒸気圧が低下
し、空気中の水分が結露するとともに、静電気が発生す
る。これにより、室内は霧がかかった状態となり、人の
避難及び救出並びに消火作業の障害になるとともに、結
露及び静電気により電子機器の絶縁不良や故障が起こ
り、重大な二次災害が発生するおそれがある。 (3) 二酸化炭素は、密度が空気よりもはるかに大きいた
め、消火対象区画内に放出された二酸化炭素は、消火対
象区画内の下部に滞留し消火効果が低下するほか、消火
対象区画内の下部の開口部から外部へ散逸しやすい。 (4) 地球温暖化に関する問題が世界的な規模で提起され
ていることから、二酸化炭素もハロンガスと同様に、将
来的には使用が制限される可能性がある。
[0006] On the other hand, fire extinguishing equipment using carbon dioxide as a fire extinguishing agent is also known to have the following problems. (1) The design concentration of carbon dioxide in the fire extinguishing target compartment at the time of fire extinguishing is about 35%. At this concentration, if there is a person in the fire extinguishing target compartment, the toxicity of carbon dioxide (narcotic ) May cause a situation involving human life. (2) In the event of a fire, carbon dioxide is sent to the injection head in a liquid state, and when it is released from the injection head into the fire extinguishing target compartment, it evaporates to a gaseous state. Saturated vapor pressure of the indoor air decreases due to deprivation of heat of vaporization, moisture in the air condenses, and static electricity is generated. As a result, the interior of the room is in a fog condition, which may hinder the evacuation and rescue of people and fire extinguishing work, and may cause insulation failure or breakdown of electronic devices due to condensation and static electricity, which may cause a serious secondary disaster. is there. (3) Since carbon dioxide has a much higher density than air, the carbon dioxide released into the fire extinguishing compartment stays in the lower part of the fire extinguishing compartment and the fire extinguishing effect is reduced. It is easy to dissipate outside through the lower opening. (4) As the issue of global warming is raised on a global scale, the use of carbon dioxide may be restricted in the future, as with halon gas.

【0007】[0007]

【発明が解決しようとする課題】ところで、本件出願人
は、上記従来のガス系消火設備が有する多くの問題点を
解決するために、先に窒素ガスや窒素ガスに、オゾン層
を破壊しないパーフルオロアルカン(パーフルオロブタ
ン(C4F10))、ハイドロジェノフルオロアルカン
(トリフルオロメタン(CHF3)、へプタフルオロプ
ロパン(C3HF7)又はペンタフルオロエタン(C2H
F5))又はハイドロジェノフルオロハロゲノアルカン
(アイオドトリフルオロメタン(CF3I))(以下、
これらを総称して「フッ素系化合物」という。)の少な
くとも1種類を10容積%以下の割合で混合した混合ガ
ス(以下単に「混合ガス」という。)を消火剤として使
用する消火設備を提案した(特願平6ー312690号
及び特願平7ー77374号)。
By the way, the applicant of the present invention has proposed to solve the above-mentioned many problems of the conventional gas fire extinguishing system by first adding nitrogen gas or nitrogen gas to a gas that does not destroy the ozone layer. Fluoroalkane (perfluorobutane (C4F10)), hydrogenofluoroalkane (trifluoromethane (CHF3), heptafluoropropane (C3HF7) or pentafluoroethane (C2H
F5)) or hydrogenofluorohalogenoalkane (iodotrifluoromethane (CF3I)) (hereinafter referred to as
These are collectively referred to as "fluorine compounds". (Japanese Patent Application Nos. 6-31690 and 6-313690) have proposed a fire extinguishing system using a mixed gas (hereinafter, simply referred to as a "mixed gas") obtained by mixing at least one of the above types in a proportion of 10% by volume or less. No. 7-77374).

【0008】しかしながら、ガス系消火設備の消火剤と
して窒素ガスや混合ガスを使用した場合も、以下の問題
点があることがわかった。 (1) ガス系消火設備の消火剤としての窒素ガスや混合ガ
スは、加圧してガス状態で貯蔵されたものを使用するた
め、加圧液化した状態で貯蔵されたものを使用する二酸
化炭素やハロンガスに比べて、同容積の消火対象区画の
消火に要する消火剤ガス貯蔵容器の数が数倍必要とな
り、消火剤ガス貯蔵容器の大きな設置スペースが必要と
なる。 (2) 設置する消火剤ガス貯蔵容器の数を低減するために
は、消火剤ガス貯蔵容器に充填する不活性消火剤ガスの
充填圧力を高める必要があるが、不活性消火剤ガスの充
填圧力を高めた場合、選択弁、主配管、枝管、噴射ヘッ
ド等の消火設備の二次側機器にも不活性消火剤ガスの高
いガス圧がかかることとなり、このため、これら二次側
機器の耐圧グレードを上げる必要があり、設備費が著し
く高くなり、また、既存の設備には、適用できない。
However, it has been found that the following problems also occur when nitrogen gas or mixed gas is used as a fire extinguishing agent for gas fire extinguishing equipment. (1) Nitrogen gas or mixed gas as a fire extinguishing agent for gas fire extinguishing equipment is used under pressure and stored in gaseous state. Compared with halon gas, the number of fire extinguisher gas storage containers required for extinguishing a fire extinguishing target compartment of the same volume is several times larger, and a large installation space for fire extinguisher gas storage containers is required. (2) In order to reduce the number of fire extinguishing agent gas storage containers to be installed, it is necessary to increase the filling pressure of inert fire extinguishing agent gas to be filled in the fire extinguishing agent gas storage container. When the pressure is increased, the secondary pressure of the fire extinguishing equipment such as the selection valve, the main pipe, the branch pipe, and the injection head is also subject to the high gas pressure of the inert fire extinguishing agent gas. It is necessary to increase the pressure resistance grade, which significantly increases equipment costs, and is not applicable to existing equipment.

【0009】本発明は、消火剤として窒素ガスや混合ガ
ス等の消火剤ガス貯蔵容器内にガス状態で貯蔵される不
活性消火剤ガスを使用するガス系消火設備の有する問題
点に鑑み、高圧の供給側ガス圧を所定の出口側ガス圧に
減圧することができ、これにより、例えば、ガス系消火
設備に適用した場合に、ガス系消火設備の二次側機器の
耐圧グレードを上げずに不活性消火剤ガスの充填圧力を
高めることができるガス系消火設備用減圧装置を提供す
ることを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the problems of a gas fire extinguishing system using an inert fire extinguishing gas stored in a gaseous state in a fire extinguishing gas storage container such as a nitrogen gas or a mixed gas as a fire extinguishing agent. The supply-side gas pressure of the gas can be reduced to a predetermined outlet-side gas pressure, thereby, for example, when applied to gas-based fire extinguishing equipment, without increasing the pressure-resistant grade of the secondary equipment of the gas-based fire extinguishing equipment. An object of the present invention is to provide a pressure reducing device for gas fire extinguishing equipment that can increase the filling pressure of an inert fire extinguishing agent gas.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するた
め、本発明の減圧装置は、消火剤ガス貯蔵容器内にガス
状態で貯蔵されている不活性消火剤ガスを消火対象区画
内に放出し、消火対象区画内の消火剤の濃度を消炎濃度
以上に維持することによって消火するようにしたガス系
消火設備の消火剤ガス貯蔵容器の容器弁を兼ねた減圧装
置において、両側の受圧面に供給側ガス圧及び出口側ガ
ス圧がそれぞれ所定の面積割合でかかるように構成した
ガス流路に配設した流路弁と、一方の受圧面に基準ガス
圧が、他方の受圧面に出口側ガス圧がかかるように構成
するとともに、前記他方の受圧面に流路弁をガス流路の
ガス出口側から操作する操作棒を突設したピストンとを
備え、ガス流路のガス供給側をガス貯蔵容器に直結し、
ガス流路を閉鎖する方向に前記流路弁を付勢することに
より、前記ピストンの一方の受圧面に基準ガス圧がかか
らない場合にガス流路を閉鎖するばねを配設したことを
特徴とする。
In order to achieve the above object, a pressure reducing apparatus according to the present invention discharges an inert fire extinguishing agent gas stored in a gaseous state in a fire extinguishing agent gas storage container into a fire extinguishing target compartment. In a decompression device that also serves as a container valve of a fire extinguisher gas storage container of a gas fire extinguishing system that extinguishes the fire by maintaining the concentration of the fire extinguishing agent in the fire extinguishing compartment equal to or higher than the flame-extinguishing concentration, it is supplied to both pressure receiving surfaces. A flow path valve disposed in a gas flow path configured such that a side gas pressure and an outlet side gas pressure are applied at a predetermined area ratio, a reference gas pressure on one pressure receiving surface, and an outlet gas on the other pressure receiving surface. A piston having an operation rod for operating a flow path valve from the gas outlet side of the gas flow path on the other pressure receiving surface, and a gas storage side of the gas flow path. Directly connected to the container,
A spring for closing the gas flow path when a reference gas pressure is not applied to one of the pressure receiving surfaces of the piston by urging the flow path valve in a direction to close the gas flow path is provided. .

【0011】本発明のガス系消火設備用減圧装置は、消
火剤ガス貯蔵容器内にガス状態で貯蔵されている不活性
消火剤ガスを消火対象区画内に放出し、消火対象区画内
の消火剤の濃度を消炎濃度以上に維持することによって
消火するようにしたガス系消火設備の消火剤ガス貯蔵容
器の容器弁を兼ねた減圧装置のガス流路に配設した流路
弁の両側の受圧面に供給側ガス圧及び出口側ガス圧がそ
れぞれ所定の面積割合でかかるように構成することによ
り、高圧の供給側ガス圧を所定の出口側ガス圧に減圧す
る減圧装置を、コンパクトな構造により実現することが
でき、また、出口側ガス圧の値を基準ガス圧を変えるこ
とによって広い範囲で、かつ、高精度に調整することが
できる。このため、この減圧装置を適用したガス系消火
設備は、消火設備の二次側機器の耐圧グレードを上げる
ことなく不活性消火剤ガスの充填圧力を高めることがで
きるとともに、供給側ガス圧が低下した場合でも、不活
性消火剤ガスの放出量を一定に保つことができる。
The decompression device for gas fire extinguishing equipment according to the present invention discharges an inert fire extinguishing gas stored in a gaseous state in a fire extinguishing agent gas storage container into a fire extinguishing target compartment, and extinguishes the fire extinguishing agent in the fire extinguishing target compartment. Pressure-receiving surfaces on both sides of a flow path valve provided in the gas flow path of a pressure reducing device that also serves as a container valve of a fire extinguisher gas storage container of a gas fire extinguishing system that extinguishes a fire by maintaining the concentration of the fire extinguishing concentration at or above the quenching concentration By using a configuration in which the supply gas pressure and the outlet gas pressure are applied at predetermined area ratios, a pressure reducing device that reduces the high-pressure supply gas pressure to the predetermined outlet gas pressure is realized with a compact structure. In addition, the value of the outlet side gas pressure can be adjusted in a wide range and with high accuracy by changing the reference gas pressure. For this reason, the gas fire extinguishing equipment to which this pressure reducing device is applied can increase the filling pressure of the inert fire extinguishing agent gas without increasing the pressure resistance grade of the secondary equipment of the fire extinguishing equipment and reduce the supply gas pressure. Even in this case, the amount of the inert fire extinguishing agent gas released can be kept constant.

【0012】さらに、ガス流路のガス供給側をガス貯蔵
容器に直結し、ガス流路を閉鎖する方向に流路弁を付勢
することにより、ピストンの一方の受圧面に基準ガス圧
がかかっていない場合にガス流路を閉鎖するばねを配設
するようにしているので、減圧装置を容器弁として用い
ることができる。
Further, the reference gas pressure is applied to one pressure receiving surface of the piston by directly connecting the gas supply side of the gas flow path to the gas storage container and biasing the flow path valve in a direction to close the gas flow path. Since a spring that closes the gas flow path is provided when it is not, the pressure reducing device can be used as a container valve.

【0013】[0013]

【発明の実施の形態】以下、本発明の減圧装置の実施の
形態を図面に示すガス系消火設備に基づいて説明する。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, an embodiment of a pressure reducing device according to the present invention will be described based on a gas fire extinguishing system shown in the drawings.

【0014】図1に、本発明の減圧装置を用いたガス系
消火設備の一例を示す。本例は、3つの消火対象区画6
−1,6−2,6−3を有する場合のガス系消火設備を
示したものである。このガス系消火設備は、不活性消火
剤ガスとして、例えば、窒素ガスを使用し、これを加圧
して高圧ガス容器に充填した状態(35℃において、1
80kgf/cm2)で消火設備内に保管することにより、消
火剤ガス貯蔵容器1として利用する。本例のガス系消火
設備には、5本の消火剤ガス貯蔵容器1−1,1−2,
・・・1−5を備え、各容器1には、容器弁2を介して
連結管3を接続し、さらに連結管3を1本の集合管4に
接続し、この集合管4を各消火対象区画6−1,6−
2,6−3まで延設した主配管5−1,5−2,5−3
に接続する。主配管5−1,5−2,5−3には、選択
弁9−1,9−2,9−3を配設し、消火対象区画6−
1,6−2,6−3に選択的に不活性消火剤ガスを送る
ようにする。消火対象区画6−1,6−2,6−3まで
延設した主配管5−1,5−2,5−3を、消火対象区
画6−1,6−2,6−3内にそれぞれ配設した枝管8
−1,8−2,8−3に接続し、この枝管8−1,8−
2,8−3を消火対象区画6−1,6−2,6−3内の
適所に複数個配設した噴射ヘッド7−1,7−2,7−
3に接続する。
FIG. 1 shows an example of a gas fire extinguishing system using the pressure reducing device of the present invention. In this example, three fire extinguishing target sections 6
This shows a gas fire extinguishing system in the case of having -1, 6-2, and 6-3. This gas fire extinguishing system uses a nitrogen gas, for example, as an inert fire extinguishing agent gas, pressurizes it and fills a high-pressure gas container (at 35 ° C., 1
It is used as a fire extinguisher gas storage container 1 by storing it in a fire extinguishing system at 80 kgf / cm 2 ). In the gas fire extinguishing system of this example, five fire extinguisher gas storage containers 1-1, 1-2,
.. Provided with 1-5, a connecting pipe 3 is connected to each container 1 via a container valve 2, and further the connecting pipe 3 is connected to one collecting pipe 4, and this collecting pipe 4 is Target sections 6-1 and 6
Main pipes 5-1, 5-2, 5-3 extended to 2, 6-3
Connect to Select valves 9-1, 9-2, and 9-3 are provided in the main piping 5-1, 5-2, and 5-3, and the fire extinguishing target section 6--6 is provided.
An inert fire extinguishing agent gas is selectively sent to 1, 6-2 and 6-3. The main pipes 5-1, 5-2 and 5-3 extending to the fire extinguishing sections 6-1, 6-2 and 6-3 are respectively placed in the fire extinguishing sections 6-1, 6-2 and 6-3. Branch pipe 8 arranged
-1, 8-2, 8-3, and the branch pipes 8-1, 8-
Injection heads 7-1, 7-2, 7- in which a plurality of 2,8-3 are arranged at appropriate places in fire extinguishing sections 6-1, 6-2, 6-3.
Connect to 3.

【0015】ところで、通常、各消火対象区画6−1,
6−2,6−3は、その容積が異なるため、当然、消火
するのに必要となる不活性消火剤ガスの量も異なる。こ
のため、主配管5−1,5−2,5−3の口径を各消火
対象区画6−1,6−2,6−3の容積に応じて異なら
せるほか、火災の際、消火対象となる消火対象区画6−
1,6−2,6−3に対応した本数の消火剤ガス貯蔵容
器1が開放されるようにガス系消火設備を構成する。
In general, each fire extinguishing section 6-1
Since 6-2 and 6-3 have different volumes, the amount of the inert fire extinguisher gas required to extinguish the fire naturally differs. For this reason, the diameters of the main pipes 5-1, 5-2, 5-3 are made different according to the volumes of the fire extinguishing sections 6-1, 6-2, 6-3. Fire extinguishing area 6
The gas fire extinguishing system is configured so that the number of fire extinguisher gas storage containers 1 corresponding to 1, 6-2 and 6-3 is opened.

【0016】ここで、開放すべき消火剤ガス貯蔵容器1
の本数を、消火対象区画6−1が5本、消火対象区画6
−2が3本、消火対象区画6−3が1本に設定すること
とする。なお、図中、9−1,9−2,9−3は選択
弁、10−1,10−2,10−3は選択弁開放装置、
11−1,11−2,11−3は起動用ガス容器、12
−1,12−2,12−3は起動用ガス容器開放用のソ
レノイドである。また、図中、13−1,13−2,1
3−3は、選択弁9−1,9−2,9−3及び起動用ガ
ス容器11−1,11−2,11−3の開放をコントロ
ールする起動用ガス管路で、選択弁開放装置10−1,
10−2,10−3に接続され、その途中の適所に不還
弁14−1,14−2,14−3,14−A,14−B
を配設する。なお、不還弁14−1,14−2,14−
3,14−A,14−Bの通過可能方向は、図の矢印の
向きで表している。なお、これらの部材の末尾の数字
1,2,3は、消火対象区画の末尾の数字1,2,3に
それぞれ対応している。
Here, the fire extinguisher gas storage container 1 to be opened
The number of fire extinguishing sections 6-1 is 5
-2 is set to three, and the fire extinguishing target section 6-3 is set to one. In the figure, 9-1, 9-2, 9-3 are selection valves, 10-1, 10-2, 10-3 are selection valve opening devices,
11-1, 11-2, 11-3 are starting gas containers,
Reference numerals -1, 12-2, and 12-3 denote solenoids for opening the starting gas container. In the figure, 13-1, 13-2, 1
Reference numeral 3-3 denotes a starting gas pipeline for controlling the opening of the selection valves 9-1, 9-2, 9-3 and the starting gas containers 11-1, 11-2, 11-3. 10-1,
10-2, 10-3, and non-return valves 14-1, 14-2, 14-3, 14-A, 14-B at appropriate places along the way.
Is arranged. In addition, non-return valves 14-1, 14-2, 14-
Passable directions of 3, 14-A and 14-B are indicated by directions of arrows in the figure. The numbers 1, 2, and 3 at the end of these members respectively correspond to the numbers 1, 2, and 3 at the end of the fire extinguishing target section.

【0017】この場合において、容器弁2には、図2に
示す、高圧の供給側ガス圧P0を定圧ガス源からの基準
ガス圧P1によって規定される所定の出口側ガス圧P2に
減圧することができる本発明に係る減圧装置を用いる。
この減圧装置2は、両側の受圧面にガス流路21のガス
供給側21aから供給側ガス圧P0が、また、ガス流路
21のガス出口側21bから(図2において下方の受圧
面には出口側ガス供給流路21cを介して)出口側ガス
圧P2がそれぞれ所定の面積割合でかかるように構成し
たガス流路21に配設した流路弁22と、ガス流路21
を閉鎖する方向に流路弁22を付勢するばね23と、一
方の受圧面に定圧ガス源(本例の場合は、定圧ガス源と
して、窒素ガスを充填(35℃において、110kgf/c
m2)した起動用ガス容器11−1,11−2,11−3
を利用するようにしている。)から定圧ガス供給流路2
4を介して基準ガス圧P1が、他方の受圧面にガス出口
側21bから出口側ガス供給流路21dを介して出口側
ガス圧P2がかかるように構成するとともに、他方の受
圧面に流路弁22を操作する操作棒27を突設したピス
トン26と、流路弁22の方向とは逆方向にピストン2
6を付勢するばね28とからなる。この場合において、
減圧装置2は、ガス貯蔵容器1に直結するようにしたガ
ス流路21のガス供給側21aを構成するガス供給側本
体20aと、ガス流路21のガス出口側21b及び弁座
29を構成するガス出口側本体20bと、定圧ガス供給
流路24及びピストン26を収容するシリンダ25を構
成する定圧ガス供給流路側本体20cとからなり、これ
らを一体的に組み立てて構成するようにしている。
In this case, the high pressure supply gas pressure P0 shown in FIG. 2 is reduced to a predetermined outlet gas pressure P2 defined by the reference gas pressure P1 from the constant pressure gas source. The pressure reducing device according to the present invention is used.
The depressurizing device 2 has a supply-side gas pressure P0 from the gas supply side 21a of the gas passage 21 on the pressure-receiving surfaces on both sides, and a gas outlet side 21b from the gas passage 21 (the lower pressure-receiving surface in FIG. A flow path valve 22 disposed in a gas flow path 21 configured such that an outlet side gas pressure P2 is applied at a predetermined area ratio (via an outlet side gas supply flow path 21c);
A spring 23 for urging the flow path valve 22 in the direction to close the valve, and a constant-pressure gas source (in this case, a nitrogen gas is charged as a constant-pressure gas source at 110 ° C at 35 ° C.
m 2 ) Startup gas containers 11-1, 11-2, 11-3
I use it. ) To constant pressure gas supply channel 2
4, a reference gas pressure P1 is applied to the other pressure receiving surface from the gas outlet side 21b via the outlet gas supply flow path 21d, and an outlet gas pressure P2 is applied to the other pressure receiving surface. A piston 26 provided with an operation rod 27 for operating the valve 22;
And a spring 28 for biasing the spring 6. In this case,
The decompression device 2 forms a gas supply side main body 20 a that forms a gas supply side 21 a of a gas flow path 21 that is directly connected to the gas storage container 1, and forms a gas outlet side 21 b and a valve seat 29 of the gas flow path 21. It comprises a gas outlet side main body 20b and a constant pressure gas supply flow path side main body 20c constituting a cylinder 25 accommodating the constant pressure gas supply flow path 24 and the piston 26, and these are integrally assembled and configured.

【0018】次に、この減圧装置2の動作について説明
する。定圧ガス源としての起動用ガス容器11−1,1
1−2,11−3から定圧ガス供給流路24に基準ガス
圧P1(110kgf/cm2)の窒素ガスを供給することに
より、ピストン26をばね28の付勢力に抗して移動さ
せ、ピストン26の受圧面に突設した操作棒27により
流路弁22をばね23の付勢力に抗して操作し、ガス流
路21を開放させる。ガス流路21が開放されると、消
火剤ガス貯蔵容器1からガス流路21のガス出口側21
bに不活性消火剤ガスが流入するが、減圧装置2は、流
路弁22の両側の受圧面に、消火剤ガス貯蔵容器1内の
不活性消火剤ガスの供給側ガス圧P0(35℃におい
て、180kgf/cm2)及び出口側ガス圧P2が、また、
ピストン26の一方の受圧面に定圧ガス源からの基準ガ
ス圧P1(35℃において、110kgf/cm2)が、他方
の受圧面に出口側ガス圧P2が、それぞれ所定の面積割
合でかかるように構成されているため、下記の式(1)
に従って流路弁22及びピストン26は、瞬時に平衡
し、本例の場合、表1及び表2に示すように、出口側ガ
ス圧P2は、起動用ガス容器11−1,11−2,11
−3の基準ガス圧P1(110kgf/cm2)と略等しい値
に保持される。なお、表1及び表2の出口側ガス圧P2
は、式(1)から導出した式(2)により算出した数値
である。 (A2−C2)P0+(C2+B2)P2=B2・P1+A2・P2 ・・・(1) P2=(B2・P1−(A2−C2)P0)/(C2+B2−A2)・・・(2) ここで、Aは、弁座29の直径、Bは、ピストン26の
直径、Cは、流路弁22の出口側ガス圧P2がかかる下
方の受圧面の直径である。この場合において、減圧装置
2によって保持される出口側ガス圧P2は、定圧ガス
源、すなわち、起動用ガス容器11−1,11−2,1
1−3の基準ガス圧P1自体を調整したり、起動用ガス
容器11−1,11−2,11−3に圧力調整器を配設
し、この圧力調整器により基準ガス圧P1を調整した
り、流路弁22及びピストン26の形状を異ならせるこ
と等により変更することができるが、不活性ガス消火設
備の設計上、出口側ガス圧P2が基準ガス圧P0と略等し
い値に保持されるように構成することが望ましい。な
お、この減圧装置2は、定圧ガス源、すなわち、起動用
ガス容器11−1,11−2,11−3からの窒素ガス
の供給を停止するとともに、定圧ガス供給流路24内の
窒素ガスを排出することにより、ガス流路21を閉鎖す
ることができる機能を有するものであり、この機能を利
用して、一旦開放した消火剤ガス貯蔵容器を閉鎖するよ
うに構成することも可能である。
Next, the operation of the pressure reducing device 2 will be described. Starting gas container 11-1, 1 as a constant pressure gas source
By supplying nitrogen gas at a reference gas pressure P1 (110 kgf / cm 2 ) from the 1-2 and 11-3 to the constant-pressure gas supply flow path 24, the piston 26 is moved against the urging force of the spring 28, The gas flow path 21 is opened by operating the flow path valve 22 against the urging force of the spring 23 by the operation rod 27 projecting from the pressure receiving surface 26. When the gas flow path 21 is opened, the fire extinguisher gas storage container 1 moves from the gas discharge side 21 to the gas outlet side 21 of the gas flow path 21.
b, the depressurizing device 2 applies the supply-side gas pressure P0 (35 ° C.) of the inert fire-extinguishing gas in the fire-extinguishing-gas storage container 1 to the pressure-receiving surfaces on both sides of the flow path valve 22. At 180 kgf / cm 2 ) and the outlet gas pressure P 2 ,
A reference gas pressure P1 (110 kgf / cm 2 at 35 ° C.) from the constant pressure gas source is applied to one of the pressure receiving surfaces of the piston 26, and an outlet gas pressure P2 is applied to the other pressure receiving surface at a predetermined area ratio. The following equation (1)
Accordingly, the flow path valve 22 and the piston 26 equilibrate instantaneously, and in this example, as shown in Tables 1 and 2, the outlet gas pressure P2 is set to the starting gas containers 11-1, 11-2, 11
Is held substantially equal to the -3 of the reference gas pressure P1 (110kgf / cm 2). The outlet gas pressure P2 in Tables 1 and 2
Is a numerical value calculated by Expression (2) derived from Expression (1). (A 2 −C 2 ) P 0 + (C 2 + B 2 ) P 2 = B 2 · P 1 + A 2 · P 2 (1) P 2 = (B 2 · P 1 − (A 2 −C 2 ) P 0) / (C 2 + B 2 −A 2 ) (2) where A is the diameter of the valve seat 29, B is the diameter of the piston 26, and C is the lower pressure receiving the gas pressure P 2 on the outlet side of the flow path valve 22. The diameter of the surface. In this case, the outlet gas pressure P2 held by the pressure reducing device 2 is a constant pressure gas source, that is, the starting gas containers 11-1, 11-2, 1
The reference gas pressure P1 itself of 1-3 is adjusted, or a pressure regulator is provided in the starting gas containers 11-1, 11-2, and 11-3, and the reference gas pressure P1 is adjusted by the pressure regulator. However, due to the design of the inert gas fire extinguishing equipment, the outlet side gas pressure P2 is maintained at a value substantially equal to the reference gas pressure P0. It is desirable to configure so that. The decompression device 2 stops the supply of the nitrogen gas from the constant-pressure gas source, that is, the nitrogen gas from the start-up gas containers 11-1, 11-2, and 11-3. Is discharged, so that the gas flow path 21 can be closed. By using this function, the fire extinguishing agent gas storage container that has been opened can be closed. .

【0019】[0019]

【表1】 [Table 1]

【0020】[0020]

【表2】 [Table 2]

【0021】そして、この減圧装置2は、表1及び表2
に示すように、消火剤ガス貯蔵容器1内の不活性消火剤
ガスの圧力、すなわち、供給側ガス圧P0が、基準ガス
圧P1以下に低下するまでは、出口側ガス圧P2を基準ガ
ス圧P1と略等しい値に保持する機能を有しているた
め、不活性消火剤ガスの放出により消火剤ガス貯蔵容器
内の不活性消火剤ガスの圧力が低下した場合でも、出口
側ガス圧P2を基準ガス圧P1と略等しい値に維持するこ
とにより、不活性消火剤ガスの放出量を一定に保つこと
ができる。
The decompression device 2 is shown in Tables 1 and 2
As shown in FIG. 2, the outlet gas pressure P2 is maintained at the reference gas pressure until the pressure of the inert fire-extinguishing gas in the fire-extinguishing gas storage container 1, that is, the supply gas pressure P0 falls below the reference gas pressure P1. Since it has a function of maintaining a value substantially equal to P1, even when the pressure of the inert fire-extinguishing gas in the fire-extinguishing gas storage container is reduced by the release of the inert fire-extinguishing gas, the outlet-side gas pressure P2 is reduced. By maintaining the gas pressure at a value substantially equal to the reference gas pressure P1, the discharge amount of the inert fire extinguishing agent gas can be kept constant.

【0022】次に、この減圧装置2を容器弁として用い
た上記のガス系消火設備の火災の際の動作について説明
する。いま、消火対象区画6−1に火災が発生したとす
れば、火災発見者がこの消火対象区画6−1に対応する
押釦(手動操作の場合)を操作すると、電気信号が起動
用ガス容器開放用のソレノイド12−1に送られ、ソレ
ノイド12−1が動作して起動用ガス容器11−1が開
放される。起動用ガス容器11−1が開放されることに
より放出された起動用ガスは、まず、選択弁開放装置1
0−1に導入されて選択弁9−1を開放してから、不還
弁14−1を経て起動用ガス管路13−1を通り、不還
弁14−A及び不還弁14−Bを通過して全ての容器弁
2に至って消火剤ガス貯蔵容器1を5本とも開放する。
このとき、不還弁14−2及び不還弁14−3を通過す
ることができないため、選択弁9−2及び選択弁9−3
は開放されない。ところで、容器弁2には、高圧の供給
側ガス圧P0を定圧ガス源からの基準ガス圧P1によって
規定される所定の出口側ガス圧P2に減圧することがで
きる減圧装置を用いているため、開放された5本の消火
剤ガス貯蔵容器1から基準ガス圧P1(110kgf/c
m2)以下に規制された不活性ガスが、容器弁2、連結管
3、集合管4、選択弁9−1、主配管5−1及び枝管8
−1を介して噴射ヘッド7−1まで送られ、噴射ヘッド
7−1から消火対象区画6−1内に放出される。
Next, the operation of the gas fire extinguishing system using the pressure reducing device 2 as a container valve in the event of a fire will be described. Now, assuming that a fire has occurred in the fire extinguishing target section 6-1, when a fire discoverer operates the push button (in the case of manual operation) corresponding to the fire extinguishing target section 6-1, an electric signal is output to open the starting gas container. Is sent to the solenoid 12-1, and the solenoid 12-1 operates to open the starting gas container 11-1. The start-up gas released by opening the start-up gas container 11-1 is first supplied to the selection valve opening device 1.
After being introduced at 0-1 and opening the selection valve 9-1, it passes through the nonreturn valve 14-1 and the starting gas line 13-1, passes through the nonreturn valve 14-A and the nonreturn valve 14-B. To reach all the container valves 2 to open all five fire extinguishing agent gas storage containers 1.
At this time, since it cannot pass through the non-return valve 14-2 and the non-return valve 14-3, the selection valve 9-2 and the selection valve 9-3 are not allowed.
Is not released. By the way, since the container valve 2 uses a pressure reducing device that can reduce the high-pressure supply-side gas pressure P0 to a predetermined outlet-side gas pressure P2 defined by the reference gas pressure P1 from the constant-pressure gas source, The reference gas pressure P1 (110 kgf / c) is supplied from the five opened fire extinguishing agent gas storage containers 1.
m 2 ) The inert gas regulated below is supplied to the container valve 2, the connecting pipe 3, the collecting pipe 4, the selection valve 9-1, the main pipe 5-1, and the branch pipe 8.
-1, and is discharged to the fire extinguishing section 6-1 from the jet head 7-1.

【0023】また、消火対象区画6−2に火災が発生し
たとすれば、火災発見者がこの消火対象区画6−2に対
応する押釦(手動操作の場合)を操作すると、電気信号
が起動用ガス容器開放用のソレノイド12−2に送ら
れ、ソレノイド12−2が動作して起動用ガス容器11
−2が開放される。起動用ガス容器11−2が開放され
ることにより放出された起動用ガスは、まず、選択弁開
放装置10−2に導入されて選択弁9−2を開放してか
ら、不還弁14−2を経て起動用ガス管路13−2を通
り、不還弁14−Bを通過して容器弁2に至って消火剤
ガス貯蔵容器1を3本だけ、すなわち、消火剤ガス貯蔵
容器1−3,1−4,1−5を開放する。このとき、不
還弁14−Aを通過することができないため、消火剤ガ
ス貯蔵容器1のうち2本、すなわち、消火剤ガス貯蔵容
器1−1,1−2は開放されない。また、不還弁14−
1及び不還弁14−3を通過することができないため、
選択弁9−1及び選択弁9−3は開放されない。ところ
で、容器弁2には、容器弁2には、高圧の供給側ガス圧
P0を定圧ガス源からの基準ガス圧P1によって規定され
る所定の出口側ガス圧P2に減圧することができる減圧
装置を用いているため、開放された3本の消火剤ガス貯
蔵容器1−3,1−4,1−5から基準ガス圧P1(1
10kgf/cm2)以下に規制された不活性ガスが、容器弁
2、連結管3、集合管4、選択弁9−2、主配管5−2
及び枝管8−2を介して噴射ヘッド7−2まで送られ、
噴射ヘッド7−2から消火対象区画6−2内に放出され
る。
If a fire occurs in the fire extinguishing target section 6-2, when a fire discoverer operates a push button (in the case of manual operation) corresponding to the fire extinguishing target section 6-2, an electric signal for starting is generated. It is sent to the solenoid 12-2 for opening the gas container, and the solenoid 12-2 operates to operate the gas container 11 for starting.
-2 is released. The starting gas released by opening the starting gas container 11-2 is first introduced into the selection valve opening device 10-2 to open the selection valve 9-2, and then the non-return valve 14- 2, only three fire extinguisher gas storage containers 1 pass through the starting gas pipeline 13-2, pass through the non-return valve 14-B, reach the container valve 2, ie, the fire extinguisher gas storage containers 1-3. , 1-4 and 1-5 are released. At this time, since it cannot pass through the non-return valve 14-A, two of the extinguishing agent gas storage containers 1, that is, the extinguishing agent gas storage containers 1-1 and 1-2 are not opened. In addition, non-return valve 14-
1 and cannot pass through the non-return valve 14-3,
The selection valve 9-1 and the selection valve 9-3 are not opened. By the way, the container valve 2 has a pressure reducing device that can reduce the high-pressure supply-side gas pressure P0 to a predetermined outlet-side gas pressure P2 defined by a reference gas pressure P1 from a constant-pressure gas source. , The reference gas pressure P1 (1) is supplied from the three opened fire extinguisher gas storage containers 1-3, 1-4, 1-5.
Inert gas regulated to 10 kgf / cm 2 or less is supplied to the container valve 2, the connecting pipe 3, the collecting pipe 4, the selection valve 9-2, and the main pipe 5-2.
And to the ejection head 7-2 via the branch pipe 8-2,
It is discharged from the ejection head 7-2 into the fire extinguishing target section 6-2.

【0024】また、消火対象区画6−3に火災が発生し
たとすれば、火災発見者がこの消火対象区画6−3に対
応する押釦(手動操作の場合)を操作すると、電気信号
が起動用ガス容器開放用のソレノイド12−3に送ら
れ、ソレノイド12−3が動作して起動用ガス容器11
−3が開放される。起動用ガス容器11−3が開放され
ることにより放出された起動用ガスは、まず、選択弁開
放装置10−3に導入されて選択弁9−3を開放してか
ら、不還弁14−3を経て起動用ガス管路13−3を通
り、容器弁2に至って消火剤ガス貯蔵容器1を1本だ
け、すなわち、消火剤ガス貯蔵容器1−5を開放する。
このとき、不還弁14−Bを通過することができない
(したがって、当然、不還弁14−Aも通過することが
できない)ため、消火剤ガス貯蔵容器1のうち4本、す
なわち、消火剤ガス貯蔵容器1−1,1−2,1−3,
1−4は開放されない。また、不還弁14−1及び不還
弁14−2を通過することができないため、選択弁9−
1及び選択弁9−2は開放されない。ところで、容器弁
2には、容器弁2には、高圧の供給側ガス圧P0を定圧
ガス源からの基準ガス圧P1によって規定される所定の
出口側ガス圧P2に減圧することができる減圧装置を用
いているため、開放された1本の消火剤ガス貯蔵容器1
−5から基準ガス圧P1(110kgf/cm2)以下に規制
された不活性ガスが、容器弁2、連結管3、集合管4、
選択弁9−3、主配管5−3及び枝管8−3を介して噴
射ヘッド7−3まで送られ、噴射ヘッド7−3から消火
対象区画6−3内に放出される。
If a fire occurs in the fire extinguishing target section 6-3, when a fire discoverer operates a push button (in the case of manual operation) corresponding to the fire extinguishing target section 6-3, an electric signal is generated for activation. It is sent to the solenoid 12-3 for opening the gas container, and the solenoid 12-3 operates to operate the gas container 11 for starting.
-3 is released. The starting gas released by opening the starting gas container 11-3 is first introduced into the selection valve opening device 10-3 to open the selection valve 9-3, and then the non-return valve 14- After passing through 3 and passing through the starting gas line 13-3 and reaching the container valve 2, only one extinguishing agent gas storage container 1 is opened, that is, the extinguishing agent gas storage container 1-5 is opened.
At this time, since the gas cannot pass through the non-return valve 14-B (and, of course, cannot also pass through the non-return valve 14-A), four of the fire-extinguishing agent gas storage containers 1, Gas storage containers 1-1, 1-2, 1-3,
1-4 are not released. Further, since the gas cannot pass through the non-return valve 14-1 and the non-return valve 14-2, the selection valve 9-
1 and the selection valve 9-2 are not opened. By the way, the container valve 2 has a pressure reducing device that can reduce the high-pressure supply-side gas pressure P0 to a predetermined outlet-side gas pressure P2 defined by a reference gas pressure P1 from a constant-pressure gas source. , One open fire extinguisher gas storage container 1
An inert gas regulated to a reference gas pressure P1 (110 kgf / cm 2 ) or lower from −5 is supplied to the container valve 2, the connecting pipe 3, the collecting pipe 4,
It is sent to the injection head 7-3 via the selection valve 9-3, the main pipe 5-3, and the branch pipe 8-3, and is discharged from the injection head 7-3 into the fire extinguishing target section 6-3.

【0025】以上、消火対象区画が3区画で、消火剤ガ
ス貯蔵容器1の本数が5本の場合を例にして説明した
が、消火対象区画の数及び消火剤ガス貯蔵容器1の本数
並びに開放される消火剤ガス貯蔵容器1の本数は、本実
施例(以下に示す第2実施例及び第3実施例も同様。)
のものに限定されるものではなく、必要に応じて任意に
設定することができる。
In the above, the case where the number of fire extinguisher compartments is three and the number of fire extinguisher gas storage containers 1 is five has been described as an example. The number of fire extinguishing agent gas storage containers 1 to be performed is the same as in the present embodiment (the same is applied to the second embodiment and the third embodiment described below).
The present invention is not limited to this, and can be set arbitrarily as needed.

【0026】本発明の減圧装置2は、ガス流路21に配
設した流路弁22の両側の受圧面に供給側ガス圧P0及
び出口側ガス圧P2がそれぞれ所定の面積割合でかかる
ように構成することにより、減圧装置をコンパクトな構
造とすることができ、また、出口側ガス圧P2の値を基
準ガス圧P1を変えることによって広い範囲で、かつ、
高精度に調整することができる(例えば、表3及び表4
に示すように、基準ガス圧P1を変えることによって、
出口側ガス圧P2を供給側ガス圧P0と比較して極めて小
さい値に保持することができる。なお、表3及び表4の
出口側ガス圧P2は、式(1)から導出した式(2)に
より算出した数値である。)ため、その適用対象は、上
記のガス系消火設備に限定されず、例えば、原子力発電
所や半導体製造工場等の設備内に定圧で各種のガスを供
給する定圧ガス供給設備等の極めて広い範囲に適用する
ことができるものである。
The pressure reducing device 2 of the present invention is arranged such that the supply gas pressure P0 and the outlet gas pressure P2 are applied to the pressure receiving surfaces on both sides of the flow path valve 22 provided in the gas flow path 21 at a predetermined area ratio. By configuring, the pressure reducing device can have a compact structure, and the value of the outlet side gas pressure P2 can be changed in a wide range by changing the reference gas pressure P1, and
It can be adjusted with high precision (for example, see Tables 3 and 4
By changing the reference gas pressure P1, as shown in
The outlet side gas pressure P2 can be kept at an extremely small value as compared with the supply side gas pressure P0. The outlet gas pressure P2 in Tables 3 and 4 is a numerical value calculated by the equation (2) derived from the equation (1). Therefore, the applicable object is not limited to the above-mentioned gas fire extinguishing equipment, but is, for example, a very wide range of constant pressure gas supply equipment for supplying various gases at a constant pressure into equipment such as a nuclear power plant or a semiconductor manufacturing plant. It can be applied to

【0027】[0027]

【表3】 [Table 3]

【0028】[0028]

【表4】 [Table 4]

【0029】[0029]

【発明の効果】本発明のガス系消火設備用減圧装置は、
消火剤ガス貯蔵容器内にガス状態で貯蔵されている不活
性消火剤ガスを消火対象区画内に放出し、消火対象区画
内の消火剤の濃度を消炎濃度以上に維持することによっ
て消火するようにしたガス系消火設備の消火剤ガス貯蔵
容器の容器弁を兼ねた減圧装置のガス流路に配設した流
路弁の両側の受圧面に供給側ガス圧及び出口側ガス圧が
それぞれ所定の面積割合でかかるように構成することに
より、高圧の供給側ガス圧を所定の出口側ガス圧に減圧
する減圧装置を、コンパクトな構造により実現すること
ができ、また、出口側ガス圧の値を基準ガス圧を変える
ことによって広い範囲で、かつ、高精度に調整すること
ができる。このため、この減圧装置を適用したガス系消
火設備は、消火設備の二次側機器の耐圧グレードを上げ
ることなく不活性消火剤ガスの充填圧力を高めることが
でき、消火剤ガス貯蔵容器の設置スペースを小さくする
ことができ、消火設備の二次側機器の耐圧グレードを上
げる必要がないことと相俟って、設備費を低廉にするこ
とができるとともに、消火設備の二次側機器の耐圧グレ
ードを上げる必要がないため、消火剤ガス貯蔵容器内に
ガス状態で貯蔵する不活性消火剤ガスを既存の設備にも
そのまま適用することができる。また、この減圧装置
は、消火剤ガス貯蔵容器内の不活性消火剤ガスの圧力、
すなわち、供給側ガス圧が、基準ガス圧以下に低下する
までは、出口側ガス圧を基準ガス圧と略等しい値に保持
する機能を有しているため、不活性消火剤ガスの放出に
より消火剤ガス貯蔵容器内の不活性消火剤ガスの圧力が
低下した場合でも、出口側ガス圧を基準ガス圧と略等し
い値に維持することにより、不活性消火剤ガスの放出量
を一定に保つことができることから、所消火設備の容量
を有効に利用することができ、設備費を低廉にすること
ができる。さらに、ガス流路のガス供給側をガス貯蔵容
器に直結し、ガス流路を閉鎖する方向に流路弁を付勢す
ることにより、ピストンの一方の受圧面に基準ガス圧が
かかっていない場合にガス流路を閉鎖するばねを配設す
るようにしているので、減圧装置を容器弁として用いる
ことができる。
The pressure reducing device for gas fire extinguishing equipment of the present invention
In order to extinguish the fire by releasing the inert fire extinguishing gas stored in gaseous state in the fire extinguishing gas storage container into the fire extinguishing target compartment and maintaining the concentration of the extinguishing agent in the fire extinguishing target compartment equal to or higher than the flame-extinguishing concentration. The supply-side gas pressure and the outlet-side gas pressure have predetermined areas on the pressure-receiving surfaces on both sides of the flow path valve provided in the gas flow path of the pressure reducing device that also serves as the container valve of the fire extinguishing agent gas storage container of the gas fire extinguishing equipment. With such a configuration, a pressure reducing device that reduces the high-pressure supply-side gas pressure to a predetermined outlet-side gas pressure can be realized with a compact structure, and the value of the outlet-side gas pressure is used as a reference. By changing the gas pressure, it can be adjusted over a wide range and with high accuracy. For this reason, gas-based fire extinguishing equipment to which this decompression device is applied can increase the filling pressure of the inert fire extinguishing gas without increasing the pressure resistance grade of the secondary equipment of the fire extinguishing equipment, and install a fire extinguishing gas storage container The space can be reduced, and it is not necessary to increase the pressure-resistant grade of the secondary equipment of the fire extinguishing equipment, so that the equipment cost can be reduced and the pressure resistance of the secondary equipment of the fire extinguishing equipment can be reduced. Since there is no need to upgrade the grade, the inert fire extinguishing agent gas stored in the gaseous state in the fire extinguishing agent gas storage container can be applied to existing equipment as it is. The decompression device also controls the pressure of the inert fire extinguishing agent gas in the fire extinguishing agent gas storage container,
That is, until the supply gas pressure falls below the reference gas pressure, the outlet gas pressure is maintained at a value substantially equal to the reference gas pressure. Even if the pressure of the inert fire extinguishing agent gas in the chemical gas storage container drops, the discharge amount of the inert fire extinguishing gas should be kept constant by maintaining the outlet gas pressure at a value approximately equal to the reference gas pressure. Therefore, the capacity of the fire extinguishing equipment can be effectively used, and the equipment cost can be reduced. Furthermore, when the reference gas pressure is not applied to one pressure receiving surface of the piston by directly connecting the gas supply side of the gas flow path to the gas storage container and urging the flow path valve in a direction to close the gas flow path. The pressure reducing device can be used as a container valve because a spring for closing the gas flow path is disposed in the container.

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

【図1】ガス系消火設備の一例を示す図である。FIG. 1 is a diagram showing an example of a gas fire extinguishing system.

【図2】本発明の減圧装置を示し、(a)はその全体断
面図、(b)はI−I線の端面図である。
2A and 2B show a decompression device according to the present invention, wherein FIG. 2A is an overall sectional view and FIG. 2B is an end view taken along line II.

【図3】ガス系消火設備の変形例を示す図である。FIG. 3 is a view showing a modification of the gas fire extinguishing equipment.

【符号の説明】[Explanation of symbols]

1 消火剤ガス貯蔵容器 2 容器弁(減圧装置) 21 ガス流路 22 流路弁 23 ばね 24 定圧ガス供給流路 25 シリンダ 26 ピストン 27 操作棒 28 ばね 29 弁座 6 消火対象区画 7 噴射ヘッド P0 供給側ガス圧 P1 基準ガス圧 P2 出口側ガス圧 REFERENCE SIGNS LIST 1 fire extinguisher gas storage container 2 container valve (pressure reducing device) 21 gas flow path 22 flow path valve 23 spring 24 constant pressure gas supply flow path 25 cylinder 26 piston 27 operating rod 28 spring 29 valve seat 6 fire extinguishing target section 7 injection head P0 supply Side gas pressure P1 Reference gas pressure P2 Outlet side gas pressure

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 消火剤ガス貯蔵容器内にガス状態で貯蔵
されている不活性消火剤ガスを消火対象区画内に放出
し、消火対象区画内の消火剤の濃度を消炎濃度以上に維
持することによって消火するようにしたガス系消火設備
の消火剤ガス貯蔵容器の容器弁を兼ねた減圧装置におい
て、両側の受圧面に供給側ガス圧(P0)及び出口側ガ
ス圧(P2)がそれぞれ所定の面積割合でかかるように
構成したガス流路(21)に配設した流路弁(22)
と、一方の受圧面に基準ガス圧(P1)が、他方の受圧
面に出口側ガス圧(P2)がかかるように構成するとと
もに、前記他方の受圧面に流路弁(22)をガス流路
(21)のガス出口側(21b)から操作する操作棒
(27)を突設したピストン(26)とを備え、ガス流
路(21)のガス供給側(21a)をガス貯蔵容器
(1)に直結し、ガス流路(21)を閉鎖する方向に前
記流路弁(22)を付勢することにより、前記ピストン
(26)の一方の受圧面に基準ガス圧(P1)がかかっ
ていない場合にガス流路(21)を閉鎖するばね(2
3)を配設したことを特徴とするガス系消火設備用減圧
装置。
1. Extinguishing an inert fire extinguishing gas stored in a gaseous state in a fire extinguishing agent gas storage container into a fire extinguishing target compartment, and maintaining the concentration of the fire extinguishing agent in the fire extinguishing target compartment equal to or higher than the flame-extinguishing concentration. In a pressure reducing device that also serves as a container valve of a fire extinguishing agent gas storage container of a gas fire extinguishing system, the supply side gas pressure (P0) and the outlet side gas pressure (P2) are respectively set to predetermined pressure receiving surfaces on both sides. A flow path valve (22) disposed in a gas flow path (21) configured to have an area ratio.
And the outlet gas pressure (P2) is applied to one pressure receiving surface and the outlet gas pressure (P2) is applied to the other pressure receiving surface. A piston (26) provided with an operation rod (27) operated from the gas outlet side (21b) of the passage (21), and the gas supply side (21a) of the gas flow path (21) is connected to the gas storage container (1). ), And the reference gas pressure (P1) is applied to one pressure receiving surface of the piston (26) by biasing the flow path valve (22) in a direction to close the gas flow path (21). A spring (2) that closes the gas flow path (21) when there is no
3) A pressure reducing device for gas fire extinguishing equipment, wherein 3) is provided.
JP16113796A 1996-05-31 1996-05-31 Decompression device for gas fire extinguishing equipment Expired - Lifetime JP2960012B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16113796A JP2960012B2 (en) 1996-05-31 1996-05-31 Decompression device for gas fire extinguishing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16113796A JP2960012B2 (en) 1996-05-31 1996-05-31 Decompression device for gas fire extinguishing equipment

Publications (2)

Publication Number Publication Date
JPH09319439A JPH09319439A (en) 1997-12-12
JP2960012B2 true JP2960012B2 (en) 1999-10-06

Family

ID=15729304

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16113796A Expired - Lifetime JP2960012B2 (en) 1996-05-31 1996-05-31 Decompression device for gas fire extinguishing equipment

Country Status (1)

Country Link
JP (1) JP2960012B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5031381B2 (en) * 2007-01-17 2012-09-19 株式会社コーアツ Pressure reducing device and gas fire extinguishing equipment using the pressure reducing device
JP5341168B2 (en) * 2011-12-19 2013-11-13 株式会社コーアツ Decompressor

Also Published As

Publication number Publication date
JPH09319439A (en) 1997-12-12

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