JPH0527089A - Emergency gas processing device for atomic reactor building - Google Patents

Emergency gas processing device for atomic reactor building

Info

Publication number
JPH0527089A
JPH0527089A JP18079491A JP18079491A JPH0527089A JP H0527089 A JPH0527089 A JP H0527089A JP 18079491 A JP18079491 A JP 18079491A JP 18079491 A JP18079491 A JP 18079491A JP H0527089 A JPH0527089 A JP H0527089A
Authority
JP
Japan
Prior art keywords
exhaust gas
outside air
activated carbon
reactor building
filter
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.)
Pending
Application number
JP18079491A
Other languages
Japanese (ja)
Inventor
Atsushi Konase
敦 木名瀬
Yasuo Kidoguchi
康夫 木戸口
Fumio Nakashita
中下文雄
Kieko Nagayama
紀衣子 長山
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.)
Hitachi Engineering and Services Co Ltd
Hitachi Ltd
Hitachi Kyowa Engineering Co Ltd
Original Assignee
Hitachi Kyowa Kogyo Ltd
Hitachi Engineering and Services Co Ltd
Hitachi 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 Hitachi Kyowa Kogyo Ltd, Hitachi Engineering and Services Co Ltd, Hitachi Ltd filed Critical Hitachi Kyowa Kogyo Ltd
Priority to JP18079491A priority Critical patent/JPH0527089A/en
Publication of JPH0527089A publication Critical patent/JPH0527089A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To improve the faculty of an activated carbon filter by adjusting the humidity of the exhaust gas passing through the activated carbon filter, in an emergency gas processing device which poocesses the exhaust gas supplied from a nuclear reactor building. CONSTITUTION:The exhaust gas supplied from a nuclear reactor building 1 is allowed to pass through a filter train 5 including an activated carbon filter 5e. An outside air take-in flow passage 7 which takes in the outside air into the filter train 5 on the upstream side of the activated carbon filter 5e during the above described passing and mixes the outside air with the exhaust gas is installed. Accordingly, the faculty of the activated carbon filter 5e can be improved by reducing the humidity of the exhaust gas passing through the activated carbon filter 5e.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、原子炉の工学的安全施
設に設けられた非常用ガス処理装置に係り、特に最適通
気条件でのその運転を可能にするための改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an emergency gas treatment device provided in an engineering safety facility of a nuclear reactor, and more particularly to an improvement for enabling its operation under optimum ventilation conditions.

【0002】[0002]

【従来の技術】従来の原子炉プラントの非常用ガス処理
装置(SGTS)は、図2に示す様に、原子炉建屋1か
ら導びかれた汚染ガスすなわち排ガス(以下、排気とも
いう)をフィルタトレイン5、排気ファン6を通して排
気筒より外部に排出する様になっている。フィルタトレ
イン5は上流側より、湿分除去装置5a、加熱コイル5
b、プレフィルタ5c、高性能粒子フィルタ5d、活性
炭フィルタ5e、高性能フィルタ5dより構成される。
2. Description of the Related Art As shown in FIG. 2, a conventional emergency gas treatment system (SGTS) for a nuclear reactor plant filters pollutant gas, that is, exhaust gas (hereinafter, also referred to as exhaust gas) introduced from a reactor building 1. It is designed to be discharged from the exhaust stack to the outside through the train 5 and the exhaust fan 6. The filter train 5 includes a moisture removing device 5a and a heating coil 5 from the upstream side.
b, pre-filter 5c, high-performance particle filter 5d, activated carbon filter 5e, and high-performance filter 5d.

【0003】湿分除去装置5aと加熱コイル5bは、湿
度調整と温度調整のために備えられている。また、プレ
フイルタ5cと高性能粒子フィルタ5dは、粒子状の放
射性物質を除去するために備えられている。活性炭フィ
ルタ5eは、主にヨウ素を添着した活性炭が使用され、
放射性ヨウ素を除去するために備えられている。尚、こ
の種の装置として関連するものは、例えば、特開昭56
−48598号等が挙げられる。
The moisture removing device 5a and the heating coil 5b are provided for humidity adjustment and temperature adjustment. Further, the prefilter 5c and the high performance particle filter 5d are provided for removing particulate radioactive substances. The activated carbon filter 5e is mainly activated carbon impregnated with iodine,
It is provided to remove radioactive iodine. A device related to this type is disclosed in, for example, Japanese Patent Laid-Open No.
No. 48598 and the like can be mentioned.

【0004】活性炭フィルタ5eに使用されているヨウ
素添着活性炭は、排ガス中に含まれている放射性ヨウ素
を吸着するために使用されている。しかし、排ガス中の
放射性ヨウ素は、無機物形態のヨウ素化合物と有機物形
態のヨウ素化合物など様々なヨウ素化合物が含まれてい
るが、活性炭フィルタに到達するヨウ素化合物として
は、無機ヨウ素(I2 )とヨウ化メチル(CH3 I)が
主成分となることが知られている。無機ヨウ素は、活性
炭へ直接吸着して除去されることが知られているが、ヨ
ウ化メチルは、活性炭への吸着能力が小さいので、式
(1)に示すように、添着された非放射性ヨウ素と同位
体交換反応を行なうことで活性炭に放射性ヨウ素が吸着
される。
The iodine-impregnated activated carbon used in the activated carbon filter 5e is used to adsorb radioactive iodine contained in the exhaust gas. However, iodine is a radioactive iodine in the exhaust gas, but contains an iodine compound and an organic material form an iodine compound such as various iodine compounds of the inorganic form, the iodine compound to reach the activated carbon filter, and an inorganic iodine (I 2) It is known that methyl chloride (CH 3 I) is the main component. It is known that inorganic iodine is directly adsorbed and removed on activated carbon, but methyl iodide has a small adsorption ability on activated carbon. Therefore, as shown in formula (1), the attached non-radioactive iodine Radioactive iodine is adsorbed on the activated carbon by performing an isotope exchange reaction with.

【0005】 CH3* +C−I → CH3 I+C−I* … (1) ここでCH3* は放射性ヨウ化メチルを示し、C−I
は活性炭と添着された非放射性ヨウ素を示し、CH3
は非放射性ヨウ化メチルを示し、C−I* は活性炭と吸
着された放射性ヨウ素を示す。
CH 3 I * + C−I → CH 3 I + C−I * (1) Here, CH 3 I * represents radioactive methyl iodide, and C−I
Represents non-radioactive iodine impregnated with activated carbon, and CH 3 I
Indicates non-radioactive methyl iodide, and C-I * indicates activated carbon and radioactive iodine adsorbed.

【0006】本反応は、温度が上昇すると反応は進み、
湿度が上がると、反応は遅くなる。また、流速が早くな
ると活性炭の吸着性能は落ちる。このため、活性炭フィ
ルタの性能を適性な能力とするため、排気の温度や湿
度、流速を適切な値にするため湿分分離器、加熱コイ
ル、除湿器等の機器が設けられている。尚、この種の装
置として関連するものには、例えば、特開昭60−19
8496、特開昭61−71399等がある。
In this reaction, when the temperature rises, the reaction proceeds,
As the humidity increases, the reaction slows down. In addition, the higher the flow rate, the lower the adsorption performance of activated carbon. Therefore, in order to bring the performance of the activated carbon filter to an appropriate capacity, equipment such as a moisture separator, a heating coil, a dehumidifier, etc. are provided in order to adjust the temperature, humidity, and flow velocity of exhaust gas to appropriate values. A device related to this type is disclosed in, for example, JP-A-60-19.
8496 and JP-A-61-71399.

【0007】他方、故障等で装置が停止したとき、装置
の流れの途中に外気を取入れて活性炭を冷却する手段を
備えた装置が、例えば、特開昭58−186098等に
示されている。
On the other hand, an apparatus provided with means for taking in outside air in the middle of the flow of the apparatus to cool the activated carbon when the apparatus stops due to a failure or the like is disclosed in, for example, Japanese Patent Laid-Open No. 186098/1983.

【0008】[0008]

【発明が解決しようとする課題】前記従来技術の非常用
ガス処理装置は、活性炭フィルタに通される排ガスの温
度や湿度、流速等の通気条件が必ずしも活性炭フィルタ
の性能を十分に発揮する通気条件になる様に運転されて
おらず、活性炭フィルタの厚さが厚くなる問題があっ
た。
SUMMARY OF THE INVENTION In the above-mentioned prior art emergency gas treatment apparatus, the ventilation conditions such as the temperature, humidity and flow velocity of the exhaust gas passed through the activated carbon filter do not necessarily exhibit the performance of the activated carbon filter. There was a problem that the thickness of the activated carbon filter became thicker because it was not operated as described above.

【0009】他方、装置の流れの途中に外気を取入れる
手段を備えた前記特開昭58−186098号に示され
た装置は、装置が停止したときに外気を取入れて活性炭
の冷却に使用しているものであって、装置の通常運転中
に外気を取入れてこれを排ガスと混合することはしてい
ないので、装置の通常運転中に排ガスの湿度を下げる作
用をするものではない。
On the other hand, the apparatus shown in the above-mentioned Japanese Patent Laid-Open No. 58-186098, which has means for taking in outside air in the middle of the flow of the apparatus, takes in outside air when the apparatus is stopped and is used for cooling activated carbon. However, since the outside air is not taken in and mixed with the exhaust gas during the normal operation of the device, it does not act to reduce the humidity of the exhaust gas during the normal operation of the device.

【0010】本発明の目的は、原子炉建屋から導かれた
排ガスを処理する非常用ガス処理装置における活性炭フ
ィルタの性能を向上するために、通気される排ガスの湿
度を適切に下げることを可能にすることにある。
An object of the present invention is to make it possible to appropriately lower the humidity of the exhaust gas that is ventilated in order to improve the performance of the activated carbon filter in the emergency gas treatment device that treats the exhaust gas introduced from the reactor building. To do.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するため
に、本発明は、原子炉建屋に対する非常用ガス処理装置
において、活性炭フィルタを含むフィルタトレインへ原
子炉建屋からの排ガス通気中に、活性炭フィルタの上流
側に上記排ガスに外気を混合する外気取入流路を設け、
以て、活性炭フィルタに導かれる排ガスの湿度を下げ、
活性炭フィルタの最も性能の出る通気条件で運転できる
ようしたものである。
In order to achieve the above object, the present invention relates to an emergency gas treatment apparatus for a reactor building, wherein activated carbon is activated during exhaust gas ventilation from the reactor building to a filter train including an activated carbon filter. An outside air intake channel for mixing outside air with the exhaust gas is provided on the upstream side of the filter,
As a result, the humidity of the exhaust gas introduced to the activated carbon filter is reduced,
It is designed so that it can be operated under the ventilation conditions that give the best performance of the activated carbon filter.

【0012】[0012]

【作用】従来、排気の温度や湿度、流速の変化に対する
添着活性炭の性能は定性的にしか知られていなかったの
で、これについて本発明者らが詳細に実験したところ次
のような性質があることが分かった。
In the past, the performance of the impregnated activated carbon with respect to changes in exhaust gas temperature, humidity, and flow velocity was known only qualitatively. Therefore, the inventors of the present invention conducted detailed experiments on this, and the following properties were obtained. I found out.

【0013】(1)温度上昇につれて吸着係数が大きく
なる(図3)。
(1) The adsorption coefficient increases as the temperature rises (FIG. 3).

【0014】(2)湿度減少につれて吸着係数が大きく
なる(図4)。
(2) The adsorption coefficient increases as the humidity decreases (FIG. 4).

【0015】(3)流速減少につれて吸着係数が大きく
なる(図5)。
(3) The adsorption coefficient increases as the flow velocity decreases (FIG. 5).

【0016】特に、(2)の性質が顕著であることから
排気の湿度を下げることが性能向上に効果的であること
が分かった。
In particular, since the property of (2) is remarkable, it has been found that reducing the humidity of exhaust gas is effective for improving the performance.

【0017】排気の除湿方法としては、次の方法が考え
られる。
The following method can be considered as a method of dehumidifying exhaust gas.

【0018】(1)加熱ヒータ等を用いて排気温度を上
げること。
(1) Raise the exhaust gas temperature by using a heater or the like.

【0019】(2)除湿器等で排気中の水分を除去する
こと。
(2) Removing moisture in exhaust gas with a dehumidifier or the like.

【0020】(3)乾燥空気を排気と混合すること。(3) Mixing dry air with exhaust air.

【0021】(1)の方法は、除湿方法として効果的で
あり、また昇温による性能向上効果をもたらす方法とし
ても好適であるが、使用している活性炭がヨウ素添着活
性炭であるため添着ヨウ素の揮発等の理由から長時間の
使用に耐えられないという問題点があり、むやみに温度
を上げられない。(2)の方法は多量の排気流量に対し
て効果的な除湿を行なうには装置が大型になるという問
題点がある。
The method (1) is effective as a dehumidifying method and is also suitable as a method of bringing about an effect of improving the performance by raising the temperature. However, since the activated carbon used is iodine impregnated activated carbon, There is a problem that it cannot be used for a long time because of volatilization, and the temperature cannot be raised unnecessarily. The method (2) has a problem in that the apparatus becomes large in size for effective dehumidification with respect to a large exhaust flow rate.

【0022】これに対して、(3)の方法では、外気の
絶対湿度が低いことから、これを排気と混合することに
より容易に排気の湿度を下げることが可能となり、ま
た、温度として最適な温度で処理することが可能であ
る。よって本発明ではこの方法を用いる。
On the other hand, in the method (3), since the absolute humidity of the outside air is low, it is possible to easily lower the humidity of the exhaust gas by mixing it with the exhaust gas, and the optimum temperature can be obtained. It is possible to treat at temperature. Therefore, this method is used in the present invention.

【0023】図6に、排気と外気の混合比と混合後の排
気の湿度との関係を示す。図6は、温度66℃、相対湿
度70%の排気ガスと、温度20℃、相対湿度50%の
外気空気を混合し、温度66℃で処理した場合である。
図6に示す様に、混合比が大きくなるに従い、相対湿度
が下げることが分かる。この条件での活性炭の性能を示
す吸着係数は、従来の処理条件では2.0であるのに対
して、混合比0.35で排気と外気とを混合した場合に
は2.27となり最高となる。これ以上の混合比で吸着
係数が下がるのは、流速が大きくなるためである。
FIG. 6 shows the relationship between the mixture ratio of the exhaust gas and the outside air and the humidity of the exhaust gas after mixing. FIG. 6 shows a case where exhaust gas having a temperature of 66 ° C. and a relative humidity of 70% is mixed with outside air having a temperature of 20 ° C. and a relative humidity of 50% and treated at a temperature of 66 ° C.
As shown in FIG. 6, it can be seen that the relative humidity decreases as the mixing ratio increases. The adsorption coefficient showing the performance of activated carbon under this condition is 2.0 under the conventional treatment conditions, whereas it is 2.27 when the exhaust gas and the outside air are mixed at a mixing ratio of 0.35, which is the highest. Become. The reason why the adsorption coefficient decreases at a mixing ratio higher than this is because the flow velocity increases.

【0024】[0024]

【実施例】以下、本発明の一実施例を図1により説明す
る。原子炉建屋1、原子炉格納容器2から吸気された排
ガスは、従来、非常用ガス処理装置のフィルタトレイン
5に直接送られていたが(図2参照)、本実施例では、
非常用ガス処理装置のフィルタトレイン5の入口ノズル
に外気取入れ口7を設け、前記排ガスと外気を0.2〜
0.5(外気/排気)の混合比で混合できる様にした。
フィルタトレイン5の構成は図2で説明したそれと同様
である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG. Exhaust gas taken in from the reactor building 1 and the reactor containment vessel 2 has been conventionally sent directly to the filter train 5 of the emergency gas treatment device (see FIG. 2).
An outside air intake port 7 is provided at the inlet nozzle of the filter train 5 of the emergency gas treatment device, and the exhaust gas and the outside air are supplied at 0.2 to
It was made possible to mix at a mixing ratio of 0.5 (outside air / exhaust air).
The structure of the filter train 5 is the same as that described with reference to FIG.

【0025】本実施例によれば、外気を混合することに
よりフィルタトレイン5に通気される排ガスの相対湿度
が下がるので非常用ガス処理装置のフィルタトレイン5
の活性炭フィルタ5eの性能を上げることができる。外
気取入れ口7を設けるだけなので構造が単純であり、安
全性が高い。また、外気入れ口7の弁は、建屋外に設置
することも可能であり、人が容易に近づいて弁操作する
ことができ、万一、電源が無くても手動操作が可能であ
り安全である。
According to this embodiment, the relative humidity of the exhaust gas aerated in the filter train 5 is lowered by mixing the outside air, so that the filter train 5 of the emergency gas treatment system is reduced.
The performance of the activated carbon filter 5e can be improved. Since only the outside air intake port 7 is provided, the structure is simple and the safety is high. Moreover, the valve of the outside air inlet 7 can be installed outside the building so that a person can easily approach it and operate the valve, and even if there is no power supply, it can be operated manually and is safe. is there.

【0026】原子炉事故直後の過渡的な排気状態の変化
(湿度、温度等の変化)や外気の気象状態の変化に対し
ては、フィルタトレイン5に入る排気と外気とのより精
密な混合比の制御が必要である。このため、制御装置を
設けた実施例を図7に示す。排気ガスの温度・湿度検出
器9と外気の温度・湿度検出器10で測定されたデータ
を制御装置8に送り、排気流量調整弁11と外気流量調
整弁12を制御することにより、フィルタトレイン5に
入る排気と外気との混合比を適正な値にする。本実施例
によれば、排気の過渡的な状態変化や気象条件に左右さ
れず、安全性の高い処理が可能となる。
For transient changes in exhaust conditions (changes in humidity, temperature, etc.) immediately after the reactor accident and changes in weather conditions of the outside air, a more precise mixing ratio of the exhaust gas entering the filter train 5 and the outside air Control is required. For this reason, an embodiment provided with a control device is shown in FIG. The data measured by the exhaust gas temperature / humidity detector 9 and the outside air temperature / humidity detector 10 are sent to the control device 8, and the exhaust flow rate adjusting valve 11 and the outside air flow rate adjusting valve 12 are controlled, whereby the filter train 5 The mixing ratio between the exhaust gas entering and the outside air is set to an appropriate value. According to the present embodiment, highly safe processing can be performed without being affected by a transitional change in exhaust gas state and weather conditions.

【0027】気象条件の変化によっては、外気の温度が
低かったり、湿度が高かったりする場合もありうる。こ
のため、図8に示す更に他の実施例では、外気取入れ口
7に外気予熱器13を設け、最適な温度条件として運転
できるようにした。排気の温度・湿度検出器9と外気の
温度・湿度検出器10の測定データにより外気予熱器1
3での加熱が制御装置8により制御される。
Depending on changes in weather conditions, the temperature of outside air may be low or the humidity may be high. Therefore, in still another embodiment shown in FIG. 8, the outside air intake port 7 is provided with the outside air preheater 13 so that it can be operated under optimum temperature conditions. The outside air preheater 1 based on the measurement data of the exhaust temperature / humidity detector 9 and the outside air temperature / humidity detector 10.
The heating at 3 is controlled by the controller 8.

【0028】これにより、活性炭フィルタ5eをより最
適な条件で働かせることができる。また、加熱コイル5
bが故障した場合のバックアップも可能となり、より安
全性の高い装置となる。
As a result, the activated carbon filter 5e can be operated under more optimal conditions. Also, the heating coil 5
Backup in case of failure of b is also possible, and the device has higher safety.

【0029】[0029]

【発明の効果】本発明によれば、フィルタトレインに入
る排気に外気を混合することにより排気相対湿度を下げ
ることができるので、活性炭の性能を上げることができ
る効果がある。
According to the present invention, since the exhaust gas relative humidity can be reduced by mixing the outside air with the exhaust gas entering the filter train, there is an effect that the performance of the activated carbon can be improved.

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

【図1】本発明の一実施例のフローシート。FIG. 1 is a flow sheet of an embodiment of the present invention.

【図2】従来装置のフローシート。FIG. 2 is a flow sheet of a conventional device.

【図3】活性炭の通気温度と放射性ヨウ素の吸着係数の
関係を示す図。
FIG. 3 is a diagram showing a relationship between an aeration temperature of activated carbon and an adsorption coefficient of radioactive iodine.

【図4】活性炭の通気湿度と放射性ヨウ素の吸着係数の
関係を示す図。
FIG. 4 is a diagram showing the relationship between the ventilation humidity of activated carbon and the adsorption coefficient of radioactive iodine.

【図5】活性炭の通気速度と放射性ヨウ素の吸着係数の
関係を示す図。
FIG. 5 is a diagram showing a relationship between an aeration rate of activated carbon and an adsorption coefficient of radioactive iodine.

【図6】外気と排気ガスとの混合比と放射性ヨウ素の吸
着係数の関係を示す図。
FIG. 6 is a diagram showing a relationship between a mixing ratio of outside air and exhaust gas and an adsorption coefficient of radioactive iodine.

【図7】本発明の他の実施例のフローシート。FIG. 7 is a flow sheet of another embodiment of the present invention.

【図8】本発明の更に他の実施例のフローシート。FIG. 8 is a flow sheet of still another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1…原子炉建屋 2…原子炉格納容
器 3…原子炉圧力容器 4…サプレッショ
ンチャンバ 5…非常用ガス処理装置のフィルタトレイン 5a…除湿器 5b…加熱コイル 5c…プレフィルタ 5d…高性能粒子
フィルタ 5e…活性炭フィルタ 6…排気ブロワ 7…外気取入れ口 8…制御装置 9…排気の温度・湿度検出器 10…外気の温度
・湿度検出器 11…排気の流量調整弁 12…外気の流量
調整弁 13…外気予熱器
DESCRIPTION OF SYMBOLS 1 ... Reactor building 2 ... Reactor containment vessel 3 ... Reactor pressure vessel 4 ... Suppression chamber 5 ... Emergency gas treatment device filter train 5a ... Dehumidifier 5b ... Heating coil 5c ... Prefilter 5d ... High performance particle filter 5e ... Activated carbon filter 6 ... Exhaust blower 7 ... Outside air intake 8 ... Control device 9 ... Exhaust air temperature / humidity detector 10 ... Outside air temperature / humidity detector 11 ... Exhaust air flow rate adjusting valve 12 ... Outside air flow rate adjusting valve 13 ... Outside air preheater

フロントページの続き (72)発明者 木戸口 康夫 茨城県日立市幸町3丁目1番1号 株式会 社日立製作所日立工場内 (72)発明者 中下文雄 茨城県日立市幸町三丁目2番2号 株式会 社日立エンジニアリングサービス内 (72)発明者 長山 紀衣子 茨城県日立市弁天町三丁目10番2号 日立 協和工業株式会社内Continued front page    (72) Inventor Yasuo Kidoguchi             3-1-1 Sachimachi Hitachi City, Ibaraki Prefecture Stock Association             Hitachi, Ltd.Hitachi factory (72) Inventor Fumio Nakashita             3-2 Sachicho, Hitachi City, Ibaraki Prefecture Stock Association             Inside Hitachi Engineering Service (72) Inventor Kiiko Nagayama             Hitachi, 3-10-3 Bentencho, Hitachi City, Ibaraki Prefecture             Kyowa Industry Co., Ltd.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 原子炉建屋からの排ガスを通気される活
性炭フィルタを含むフィルタトレインと、排気ファン
と、該フィルタトレインの下流側に連なる排気流路とか
らなる原子炉建屋非常用ガス処理装置において、フィル
タトレインへの前記排ガスの通気中に前記活性炭フィル
タの上流側に前記排ガスに外気を混合する外気取入流路
を設けたことを特徴とする原子炉建屋に対する非常用ガ
ス処理装置。
1. A reactor building emergency gas treatment device comprising a filter train including an activated carbon filter through which exhaust gas from the reactor building is ventilated, an exhaust fan, and an exhaust flow path connected to a downstream side of the filter train. An emergency gas treatment device for a nuclear reactor building, wherein an outside air intake passage for mixing outside air with the exhaust gas is provided upstream of the activated carbon filter during aeration of the exhaust gas into a filter train.
【請求項2】 外気と原子炉建屋からの排ガスとの混合
比を0.2〜0.5(外気/排気)としたことを特徴と
する請求項1記載の原子炉建屋に対する非常用ガス処理
装置。
2. The emergency gas treatment for the reactor building according to claim 1, wherein the mixing ratio of the outside air and the exhaust gas from the reactor building is 0.2 to 0.5 (outside air / exhaust gas). apparatus.
【請求項3】 外気および原子炉建屋からの排ガスの温
度、湿度又は流量を検知する手段と、これら検知された
量の変化に応じて上記排ガスと外気とを最適な混合比に
制御する制御手段とを有することを特徴とする請求項1
又は2記載の原子炉建屋に対する非常用ガス処理装置。
3. A means for detecting the temperature, humidity or flow rate of the outside air and the exhaust gas from the reactor building, and a control means for controlling the exhaust gas and the outside air to an optimum mixing ratio in accordance with changes in the detected amounts. 2. The method according to claim 1, further comprising:
Alternatively, the emergency gas treatment device for the reactor building according to 2.
【請求項4】 外気取入流路に外気予熱装置を設けたこ
とを特徴とする請求項1,2又は3記載の原子炉建屋に
対する非常用ガス処理装置。
4. The emergency gas treatment device for a reactor building according to claim 1, wherein an outside air preheating device is provided in the outside air intake passage.
JP18079491A 1991-07-22 1991-07-22 Emergency gas processing device for atomic reactor building Pending JPH0527089A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18079491A JPH0527089A (en) 1991-07-22 1991-07-22 Emergency gas processing device for atomic reactor building

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18079491A JPH0527089A (en) 1991-07-22 1991-07-22 Emergency gas processing device for atomic reactor building

Publications (1)

Publication Number Publication Date
JPH0527089A true JPH0527089A (en) 1993-02-05

Family

ID=16089455

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18079491A Pending JPH0527089A (en) 1991-07-22 1991-07-22 Emergency gas processing device for atomic reactor building

Country Status (1)

Country Link
JP (1) JPH0527089A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20210039133A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses
KR20210039132A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses
KR20210039134A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58161893A (en) * 1982-03-19 1983-09-26 株式会社東芝 Air heater control device
JPH042920A (en) * 1990-04-20 1992-01-07 Nakagawa Suiriyoku:Kk Monitoring/recording apparatus of hydraulic apparatus

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58161893A (en) * 1982-03-19 1983-09-26 株式会社東芝 Air heater control device
JPH042920A (en) * 1990-04-20 1992-01-07 Nakagawa Suiriyoku:Kk Monitoring/recording apparatus of hydraulic apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20210039133A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses
KR20210039132A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses
KR20210039134A (en) * 2019-10-01 2021-04-09 주식회사 세일에프에이 Air purification system for apartment houses

Similar Documents

Publication Publication Date Title
US6605132B2 (en) Air treatment system
JP3073466B2 (en) Air conditioning system for semiconductor clean room
EP1440695B1 (en) Device for activating oxygen from air for the destruction of VOCs and germs in closed rooms and for maintaining oxygen and ozone concentrations equal to those occuring in nature
JPS5613019A (en) Treating apparatus for electron ray irradiation exhaust gas
CN105771639A (en) Low-concentration VOC (volatile organic compound) polluted air purification device using catalyst rotating wheel
JPH0527089A (en) Emergency gas processing device for atomic reactor building
US7655077B2 (en) Air treatment system
KR20170030013A (en) Apparatus for purifying low concentration of voc-polluted air using catalytic rotor
EP1442258B1 (en) Sicherheitseinrichtung fur die luft in wenigstens einem raum eines gebaudes
JPS60125233A (en) High degree treatment of exhaust gas
CN102886183B (en) Indoor positive-pressure air cleaning device
JP2007014885A (en) Gas treating system
JP3918243B2 (en) Air conditioner with air purifying function
JP2021169097A (en) Organic solvent gas concentration device
IE42269B1 (en) Improvements in or relating to air-cleaning and ventilating devices
JP3896539B2 (en) Filter and clean room using it
JP2580375B2 (en) Clean room
JPS628202B2 (en)
JP2930446B2 (en) Atmosphere purification device in fusion reactor room
JPH11101893A (en) Iodine-removing local exhauster
JPS57174120A (en) Purifying method of waste gas
JPH0219759Y2 (en)
TWI572827B (en) Zero Energy Dissipation Device and Method for Volatile Organic Compounds
JP2554155B2 (en) Indoor air purification equipment
JPH1015051A (en) Ozone/plasma deodorizing device