JPS61280336A - Ventilating and air-conditioning facility - Google Patents

Ventilating and air-conditioning facility

Info

Publication number
JPS61280336A
JPS61280336A JP60119803A JP11980385A JPS61280336A JP S61280336 A JPS61280336 A JP S61280336A JP 60119803 A JP60119803 A JP 60119803A JP 11980385 A JP11980385 A JP 11980385A JP S61280336 A JPS61280336 A JP S61280336A
Authority
JP
Japan
Prior art keywords
carbon dioxide
air
central control
control room
ventilation
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
JP60119803A
Other languages
Japanese (ja)
Inventor
Koichiro Ooshima
大嶋 浩一郎
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP60119803A priority Critical patent/JPS61280336A/en
Publication of JPS61280336A publication Critical patent/JPS61280336A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors

Landscapes

  • Ventilation (AREA)

Abstract

PURPOSE:To permit to reduce the amount of exposure of operators in a central control chamber upon the trouble of atomic power plant by a method wherein air, whose volume is corresponding to removed carbon dioxide, is taken into the chamber in order to keep an atmospheric pressure without increasing the concentration of carbon dioxide. CONSTITUTION:Air, recirculated by emergency recirculating fans 14a, 14b and fans 3a, 3b upon the trouble of the plant, passes through a carbon dioxide removing device 20. In this case, carbon dioxide in the air is removed. Particulate suspended radioactive materials and soluble radioactive materials, remaining in the air taken into the central control chamber 2, are also removed in this case. In case the atmospheric pressure of ventilated and air-conditioned system is reduced due to the removal of carbon dioxide, isolating dampers 13a, 13b are opened and air, whose volume is corresponding to the amount of removed carbon dioxide, is taken into the chamber. Accordingly, small amount of air, taken into the central control chamber 2, may be sufficient for ventilation and the amount of exposure of the operators in the central control chamber may be reduced remarkably.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は、室内で発生する二酸化炭素を除去する換気空
調設備に関する。
DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to ventilation air conditioning equipment for removing carbon dioxide generated indoors.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

人間が室内で作業をする場合、労働安全衛生法・事務所
衛生基準規則の中で二酸化炭素濃度を0.5vo1%以
下にすることが定められているので、外気(二対して開
口部がないか、もしくは開口部があっても、十分な換気
が行なわれない場合、換気空調システムが必要となる。
When people work indoors, the Industrial Safety and Health Act and Office Hygiene Standards Regulations stipulate that the carbon dioxide concentration must be below 0.5 VO 1%. If there are openings or openings that do not provide adequate ventilation, a ventilation air conditioning system is required.

通常の場合、換気空調設備で十分に換気を行えば良いが
、特定な条件の下では、前記の規定な守れる最低の換気
しか行なえない場合がある。
Normally, ventilation and air conditioning equipment can provide sufficient ventilation, but under certain conditions, it may be possible to provide only the minimum amount of ventilation that meets the above regulations.

特定な場合には、原子力発電所中央制御室換気空調シス
テムにおける、原子力発電所事故時の換気がある。
A specific case is ventilation in nuclear power plant central control room ventilation and air conditioning systems during nuclear power plant accidents.

原子力発電所中央制御室の換気空調設備設備について、
従来例を第7図に示す。ここで第7図に従来の換気空調
装置の概要図を示す。第7図において、原子炉建屋1内
には中央制御室2が設置されている。この中央制御室2
への給気は通常時、送風機3a、3bにより原子炉建屋
1外の外気を、給気ルーパ4から吸引し、空気調和機5
a、5bを通し送風管路6を経て行なう。
Regarding the ventilation and air conditioning equipment in the nuclear power plant central control room,
A conventional example is shown in FIG. Here, FIG. 7 shows a schematic diagram of a conventional ventilation air conditioner. In FIG. 7, a central control room 2 is installed within a reactor building 1. This central control room 2
Normally, air is supplied to the air conditioner 5 by sucking outside air from outside the reactor building 1 through the air supply looper 4 using the blowers 3a and 3b.
a, 5b and the air duct 6.

中央制御室2の排気は、排気管路10を介して排風機7
a、7bにより制御室内の空気を吸引し、排気ルーパ8
から行なう。また、排気の一部は、非常用再循環管路9
を経て空気調和機5a 、 5bに至り、再び中央制御
室2内に戻される。
Exhaust air from the central control room 2 is passed through an exhaust pipe 10 to an exhaust fan 7.
The air inside the control room is sucked through a and 7b, and the exhaust looper 8
Let's do it from In addition, a part of the exhaust gas is transferred to the emergency recirculation pipe 9
The air then reaches the air conditioners 5a and 5b, and is then returned to the central control room 2.

以上の通常運転時の換気空調、1構成において、原子力
発電所で事故が発生した場合、大量の放射性物質が放出
される可能性がある。この場合、中尉性物質の放出口と
数十m程度しか離れておらず、中央制御室操作員の被曝
が問題となっている。そのため、原子力発電所事故時の
ために、中央制御室換気空調システムに非常用の系統が
設けられており、手動あるいは自動で切り替わる。この
ときの換気空調システムの機能は、中央制御室2を外気
より隔離するために、送風管路6及び排気管10等に設
けられた隔離ダンパlla、llb、12a、12b、
13a。
In one configuration of the ventilation air conditioning during normal operation, if an accident occurs at a nuclear power plant, a large amount of radioactive materials may be released. In this case, the main control room operators are exposed to radiation, which is a problem because the main control room operator is located only a few tens of meters away from the release port for the intermediate substance. Therefore, in case of a nuclear power plant accident, an emergency system is installed in the central control room ventilation and air conditioning system, which can be switched on manually or automatically. The functions of the ventilation air conditioning system at this time include isolation dampers lla, llb, 12a, 12b provided in the blower duct 6, exhaust pipe 10, etc. in order to isolate the central control room 2 from the outside air.
13a.

13bが閉じられる。中央制御室内の空気は、非常用再
循環送風機14a、14bにより吸引され、隔離ダンパ
15a、l+を介してフィルタ(活性炭フィルタ等)1
6で、空気のよごれ(タバコの煙等)が除去された後、
隔離ダンパ17a、17b 、管路9を介して空気調和
機5a、5bで温度、湿度が調節され、送風機3a。
13b is closed. The air in the central control room is sucked in by emergency recirculation blowers 14a and 14b, and passed through isolation dampers 15a and l+ to a filter (activated carbon filter, etc.) 1.
6, after the air pollution (cigarette smoke etc.) is removed,
Temperature and humidity are controlled by air conditioners 5a, 5b via isolation dampers 17a, 17b and pipe line 9, and air blower 3a.

3bによって中央制御室内に戻される。3b brings them back into the central control room.

しかし、前述した様に、室内の二酸化炭素濃度を0.5
vo1%以下に抑える必要があるため、適切に外気を取
り入れなくてはならない。次に事故時外気取入れモード
の運転状態を示す。前述の事故時の状態から隔+i;i
ダンパ13a、13bを開け、非常用再循環送風機14
a、14bにより給気ルーパ4から外気を吸引し、フィ
ルタ16を通した後、空気調和機5a、5bを経て送風
機3a、3bにより中央制御室2に給気する。一方、中
央制御室2内の空気は、隔離ダンパ12a、 12bを
開き、排風機7a、7bにより、外気取入量だけ排気ル
ーパ8から放出する。排気の一部は、非常用再循環送風
機14a、14bまたは送風機3a、3b l二吸引さ
れ、再循環する。
However, as mentioned above, if the indoor carbon dioxide concentration is reduced to 0.5
Since it is necessary to keep the VO below 1%, outside air must be brought in appropriately. Next, the operating state in the outside air intake mode at the time of an accident is shown. Distance from the state at the time of the aforementioned accident +i;i
Open the dampers 13a and 13b and turn on the emergency recirculation blower 14.
Outside air is sucked in from the air supply looper 4 by the air supply loopers 4a and 14b, passed through the filter 16, and then supplied to the central control room 2 by the blowers 3a and 3b via the air conditioners 5a and 5b. On the other hand, the air in the central control room 2 is released from the exhaust looper 8 by the amount of outside air taken in by opening the isolation dampers 12a and 12b and by the exhaust fans 7a and 7b. A portion of the exhaust air is sucked into the emergency recirculation blowers 14a, 14b or the blowers 3a, 3bl and recirculated.

フィルタ16では、粒子状で浮遊する放射性物質、放射
性よう素を除去しているため、中央制御室2内の操作員
の被曝は低減されている。しかし、放射性希ガスはフィ
ルタ16(二かからないため、1.00%が中央制御室
に送られる。また、フィルタ16のよう素除去効率は9
0%程度のものが多く、残りのよう素10%は中央制御
室2(−送られ、中央制御室操作員は被曝する恐れがあ
る。
Since the filter 16 removes radioactive substances and radioactive iodine floating in the form of particles, the exposure of operators in the central control room 2 to radiation is reduced. However, the radioactive rare gas is sent to the central control room because it does not require 2 filters (1.00% of the radioactive noble gases).
Most of the iodine is around 0%, and the remaining 10% is sent to the central control room 2 (-), where there is a risk that central control room operators may be exposed to radiation.

放射性物質の取り込み量を制限するためには、給気量を
減らせば良いが、前述した様な作業環境の規定を守れる
だけは最低限給気する必要がある。
In order to limit the amount of radioactive material taken in, it is possible to reduce the amount of air supply, but it is necessary to supply at least as much air as possible to comply with the regulations for the working environment as described above.

この給気量は、主(二酸化炭素濃度によって決ま゛、 
   −−゛ #母橋妻るが、この給気量に見合った分だけは操作員が
被、曝してしまう恐れがあった。
This air supply amount is mainly determined by the carbon dioxide concentration,
---゛# However, there was a risk that the operator would be exposed to the amount of air supplied.

〔発明の目的〕[Purpose of the invention]

本発明は以上のことを鑑みてなされたものであり、中央
制御室内の二酸化炭素濃度を確実に低下させ、中央制御
室への給気量を低減させ、操作員の被曝量を低下させる
ことができる換気空調設備を提供することを目的とする
The present invention has been made in view of the above, and is capable of reliably lowering the carbon dioxide concentration in the central control room, reducing the amount of air supplied to the central control room, and reducing the amount of radiation exposure for operators. The purpose is to provide ventilation and air conditioning equipment that can

〔発明の概要〕 本発明の換気空調設備は、給気及び排気の他に、室内空
気をプロアで吸引し、空気中の二酸化炭素を強制的に吸
着する二酸化炭素除去装置を通し、さらに残りの空気を
室内に戻す循環管路からなることを特徴とする。
[Summary of the Invention] In addition to air supply and exhaust, the ventilation air conditioning equipment of the present invention sucks indoor air with a proa, passes it through a carbon dioxide removal device that forcibly adsorbs carbon dioxide in the air, and then removes the remaining air. It is characterized by a circulation pipe that returns air to the room.

〔発明の実施例〕[Embodiments of the invention]

以下、本発明の実施例を第1図から第6図を参照して説
明する。ここで第1図(二本発明の一実施例:二係る換
気空調設備の概要図を示す。なお第7図と同一部分には
同一符号を付しその構成の説明は省略する。第1図にお
いて、換気空調設備は中央制御室2内の排気を行なう排
気管路10と中央制御室2内へ給気を行なう送風管路6
とを接続する非常用再循環管路9に二酸化炭素除去装置
20を設置して構成されている。以上の構成において、
事故時に中央制御室2が隔離される換気空調設備の運転
モードの場合、非常用再循環送風機14a、14b及び
送風機3a、3bにより再循環される空気は、二酸化炭
素除去装置20を通る。このとき、空気中の二酸化炭素
が除去される。また、中央制御室2に取り入れられた空
気に残留していた粒子状浮遊放射性物質水溶性放射性物
質も除去される。
Embodiments of the present invention will be described below with reference to FIGS. 1 to 6. Here, FIG. 1 (2) An embodiment of the present invention: A schematic diagram of a ventilation air conditioning system according to 2 is shown.The same parts as in FIG. , the ventilation air conditioning equipment includes an exhaust pipe 10 that exhausts air from the central control room 2 and a blower pipe 6 that supplies air to the central control room 2.
A carbon dioxide removal device 20 is installed in the emergency recirculation pipe 9 that connects the In the above configuration,
In the case of an operating mode of the ventilation air conditioning system in which the central control room 2 is isolated in the event of an accident, the air recirculated by the emergency recirculation blowers 14 a , 14 b and the blowers 3 a , 3 b passes through the carbon dioxide removal device 20 . At this time, carbon dioxide in the air is removed. In addition, particulate floating radioactive substances and water-soluble radioactive substances remaining in the air taken into the central control room 2 are also removed.

二酸化炭素の除去により、換気空調システム系の気圧が
低下する場合は、隔離ダンパ13a、13bを開けて、
二酸化炭素の除去岱の空気を取入れる。
If the atmospheric pressure in the ventilation air conditioning system decreases due to the removal of carbon dioxide, open the isolation dampers 13a and 13b,
Removes carbon dioxide and brings in air.

次に本発明の一実施例に係る二酸化炭素除去装置を第2
図から第5図を参照して説明する。ここで第2図(a)
に本発明の一実施例に係る二酸化炭素除去装置の第1実
施例の概略図を示し、第2図(b)に第2図(a)に示
すバブリング装置の平面図を示す。
Next, the carbon dioxide removal device according to one embodiment of the present invention was installed in a second
This will be explained with reference to FIGS. Here, Fig. 2(a)
2 shows a schematic diagram of a first embodiment of a carbon dioxide removal device according to an embodiment of the present invention, and FIG. 2(b) shows a plan view of the bubbling device shown in FIG. 2(a).

第2図において、二酸化炭素除去装置2o内は液相部と
気相部の二相となっている。二酸化炭素を除去したい気
体は、液相部に開口を持つ送風管21を通して除去タン
ク22内に送られ、送風管21の開口端につけられてい
る第2図(b)に示す小さな多数の孔が開いたバブリン
グ装置23で小径の泡となり、液相部で二酸化炭素が除
去され、気相部から排風管24を通して送出される。
In FIG. 2, the interior of the carbon dioxide removal device 2o has two phases: a liquid phase portion and a gas phase portion. The gas from which carbon dioxide is to be removed is sent into the removal tank 22 through the blast pipe 21 which has an opening in the liquid phase, and a large number of small holes shown in FIG. 2(b) attached to the open end of the blast pipe 21 are The bubbles become small in diameter in the opened bubbling device 23, carbon dioxide is removed in the liquid phase, and then sent out from the gas phase through the exhaust pipe 24.

液相部の液体は、二酸化炭素を溶解、あるいは化学反応
により吸着させるものである。
The liquid in the liquid phase dissolves carbon dioxide or adsorbs it through a chemical reaction.

この液体として、まず第1に水が使用できる。As this liquid, first of all water can be used.

二酸化炭素は、20℃、1気圧で水100m1に約90
m1溶ける。また、一部は、水と下記の反応で化合する
Carbon dioxide is about 90% in 100ml of water at 20℃ and 1 atm.
m1 melts. In addition, a part of it is combined with water in the following reaction.

co2+l12o−xn2co3  1−(、;’−1
−HCO8−(1)中央制御室2内の人数を20名、1
人当りの二酸化炭素排出量を0.02 m’/ h /
人とすると、1時間あたり約0.4rd′の水が二酸化
炭素飽和水溶液となる。
co2+l12o-xn2co3 1-(,;'-1
-HCO8- (1) Number of people in main control room 2 is 20, 1
Reduce carbon dioxide emissions per person to 0.02 m'/h/
For humans, approximately 0.4 rd' of water becomes a carbon dioxide saturated aqueous solution per hour.

従って0.4 m’/ hのペースで除去タンク22内
の水を置換すれば良い。そのために、除去タンク22に
は補給水を送れる送水管25と排水管26が設けられて
いる。
Therefore, it is sufficient to replace the water in the removal tank 22 at a pace of 0.4 m'/h. For this purpose, the removal tank 22 is provided with a water pipe 25 and a drain pipe 26 through which makeup water can be sent.

二酸化炭素の除去能力を上昇させるために、水の代りに
、二酸化炭素と化合する物質の水溶液を用いても良い。
In order to increase the carbon dioxide removal ability, an aqueous solution of a substance that combines with carbon dioxide may be used instead of water.

用いる物質としては、環基又は塩基性酸化物が考えられ
る。以下;二物質の例を示す。
The substances used may be cyclic groups or basic oxides. Below, examples of two substances are shown.

1、石灰 Ca(OH)2+C02−jcacOB↓モH,O(2
)2、水酸化ナトリウム 2NaOH+Co2−ΔNa 200B +H20(3
)3、 水酸化バリウム Ba (OH)2 + CO3−き□BaCO3+H2
0(4)4、酸化カルシウム CaO+ CO2−’= CaCO5(5)5、 酸化
マグネシウム MgO+ Co 、−1MgC0s        (
6)ここで第3図に本発明の一実施例に係る二酸化炭素
除去(二塩基性水溶液を用いた場合の二酸化炭素除去装
置の第2実施例の概略図を示す。なお、第2図(a)と
同一部分には同一符号を付しその構成の説明は省略する
。第3図において、二酸化炭素除去装置20は、除去タ
ンク22内へ送水する送水管30の上流側に薬剤タンク
31より送られる薬剤と注水管32から送られる水で作
られる水溶液を貯える薬液タンク33が設置されている
。また、実施例において、薬液タンクを削除して、二酸
化炭素除去タンクにその薬液タンクの役割を負わしても
良い。
1. Lime Ca(OH)2+C02−jcacOB↓MoH,O(2
)2, Sodium hydroxide 2NaOH+Co2-ΔNa 200B +H20(3
)3, Barium hydroxide Ba(OH)2 + CO3− □BaCO3+H2
0(4)4, Calcium oxide CaO+ CO2-'= CaCO5(5)5, Magnesium oxide MgO+ Co, -1MgC0s (
6) Here, FIG. 3 shows a schematic diagram of a second embodiment of a carbon dioxide removal device (using a dibasic aqueous solution) according to an embodiment of the present invention. The same parts as in a) are given the same reference numerals, and the explanation of the structure is omitted. In FIG. A chemical liquid tank 33 is installed to store an aqueous solution made from the chemical to be sent and the water sent from the water injection pipe 32.In addition, in the embodiment, the chemical liquid tank is deleted and the role of the chemical liquid tank is replaced by the carbon dioxide removal tank. It's okay to lose.

さらに、二酸化炭素除去タンク液相に水又は水溶液を用
いる場合に、二酸化炭素除去効果を向上させるために、
第4図に示す様な二酸化炭素除去装置を用いてもよい。
Furthermore, in order to improve the carbon dioxide removal effect when using water or an aqueous solution for the liquid phase of the carbon dioxide removal tank,
A carbon dioxide removal device as shown in FIG. 4 may also be used.

第4図において、第2図(、)と同一部分には同一符号
を付しその構成の説明は省略する。本実施例において、
除去タンク22の下部に撹はん機34が設けられ、この
撹はん機34は前記除去タンク22の下方に設けられた
撹はん機駆動装置35によって駆動されている。以上の
構成によって、より二酸化炭素の除去効果を向上させる
ことができる。
In FIG. 4, the same parts as those in FIG. In this example,
A stirrer 34 is provided below the removal tank 22, and this stirrer 34 is driven by a stirrer drive device 35 provided below the removal tank 22. With the above configuration, the effect of removing carbon dioxide can be further improved.

また、二酸化炭素除去装置として第5図に示す装置を用
いてもよい。第5図において、除去タンク40には冷凍
液(液体酸素、液体窒素等)を流入させる冷凍液送管4
1が接続され、さらにこの冷凍液を排出させる冷凍液出
口管42も接続されている。
Furthermore, the device shown in FIG. 5 may be used as the carbon dioxide removal device. In FIG. 5, a freezing liquid feed pipe 4 through which freezing liquid (liquid oxygen, liquid nitrogen, etc.) flows into a removal tank 40.
1 is connected thereto, and a refrigerant outlet pipe 42 for discharging this refrigerant is also connected.

また、二酸化炭素を除去したい気体は送風管43より導
びかれ二酸化炭素を液化させて、排液管44より排出さ
せている。そして、二酸化炭素が除去された気体は排風
管45より除去タンク40外へ導びかれる構成になって
いる。以上の構成(−よって、他の実施例と同様(二二
酸化炭素を効率良く除去させることができる。次に第6
図を参照して本発明の他の実施例に係る換気空調設備の
概要図を示す。
Further, the gas from which carbon dioxide is to be removed is led through the blast pipe 43, liquefies the carbon dioxide, and discharges it through the drain pipe 44. The gas from which carbon dioxide has been removed is guided out of the removal tank 40 through an exhaust pipe 45. The above configuration (-Therefore, similar to other embodiments) dicarbon dioxide can be removed efficiently.Next, the sixth
A schematic diagram of ventilation air conditioning equipment according to another embodiment of the present invention is shown with reference to the drawings.

なお、第7図と同一部分には同一符号を付しその構成の
説明は省略する。第6図;二おいて、中央制御室内内の
空気は送風機50により送風管51から二酸化炭素除去
装置52に送られ、二酸化炭素が除去された後、空気を
中央制御室内に戻すように構成されている。このとき、
室内の温度、湿度の調整のため、換気空調システムを起
動させて良いが、隔離モードであることが望ましい。
Note that the same parts as in FIG. 7 are given the same reference numerals, and the explanation of the structure will be omitted. In FIG. 6, the air inside the central control room is sent by a blower 50 through a blow pipe 51 to a carbon dioxide removal device 52, and after carbon dioxide is removed, the air is returned to the central control room. ing. At this time,
Ventilation and air conditioning systems may be activated to adjust indoor temperature and humidity, but it is preferable to use isolation mode.

また、二酸化炭素除去装置を、換気空調系から独立させ
る場合、除去装置を室内に置いても良い。
Moreover, when the carbon dioxide removal device is made independent from the ventilation air conditioning system, the removal device may be placed indoors.

以上の構成によって本発明の一実施例と同様の効果を得
ることができる。
With the above configuration, effects similar to those of the embodiment of the present invention can be obtained.

〔発明の効果〕〔Effect of the invention〕

仮に、室内体積を4000ツどすると、二酸化炭素の除
去を行なわなければ、約50時間で規程の0.5vo1
%濃度に達し、室内空気の入換えが必要となる。従って
50時間に4000n?の空気取込みが必要である。一
方、本発明の構成によれば二酸化炭素濃度が上昇するこ
とはなく、気圧を保つために除去した二酸化炭素の体積
分だけ、すなわち0.4 m?/ h(実施例の場合)
の取込みだけで良い。酸素の消費量は、二酸化炭素発生
分程度であるので、50時間で0.5vo1%の酸素を
消費する程度である。空気中には20%の酸素が含まれ
ているので無視しうる。
If the indoor volume is increased to 4,000 vol., it will take about 50 hours to reach the specified 0.5 vol. unless carbon dioxide is removed.
% concentration, requiring replacement of indoor air. So 4000n for 50 hours? air intake is required. On the other hand, according to the configuration of the present invention, the carbon dioxide concentration does not increase, but increases by the volume of carbon dioxide removed to maintain atmospheric pressure, that is, 0.4 m? /h (for example)
All you need to do is import it. The amount of oxygen consumed is about the same as the amount of carbon dioxide generated, so 0.5 vol% of oxygen is consumed in 50 hours. Since air contains 20% oxygen, it can be ignored.

従って、原子力発電所事故時において、中央制御室への
空気取入れ量が1/200程度で済み、大巾な中央制御
室操作員の被曝量低減が可能となる。
Therefore, in the event of a nuclear power plant accident, the amount of air taken into the central control room can be reduced to about 1/200, making it possible to significantly reduce the amount of radiation exposure of central control room operators.

また水槽を用いる場合は、空気中の浮遊放射性粒子及び
水溶性放射性物質除去の効果もあり被曝低減に寄与する
ことができる。
Furthermore, when using a water tank, it also has the effect of removing airborne radioactive particles and water-soluble radioactive substances, which can contribute to reducing radiation exposure.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例を示す換気空調設備の概要図
、第2図(a)は第1図1″−示した二酸化炭素除去装
置の第1実施例を示す概要図、第2図(blは第2図(
a)に示したバブリング装置の平面図、第3図から第5
図はそれぞれ第1図に示した二酸化炭素除去装置の第2
実施例から第4実施例を示す概要図、第6図は本発明の
他の実施例を示す換気空調設備の概要図、第7図は換気
空調設備の従来例を示す概要図である。 1・・・原子炉建屋    2・・・中央制御室3a、
3b・・・送風機    20・・・二酸化炭素除去装
置21・・・送風管      22・・・除去タンク
23・・・バブリング装置  24・・・排風管25・
・・送水管      26・・・排水管代理人 弁理
士 則 近 憩 佑(ほか1名)(a)       
          tbノ第2図 第3図 第4図 第5図
FIG. 1 is a schematic diagram of a ventilation air conditioning system showing one embodiment of the present invention, FIG. 2(a) is a schematic diagram showing a first embodiment of the carbon dioxide removal device shown in FIG. Figure (bl is Figure 2 (
Plan view of the bubbling device shown in a), Figures 3 to 5
Each figure shows the second part of the carbon dioxide removal device shown in Figure 1.
FIG. 6 is a schematic diagram showing a ventilation air conditioning system according to another embodiment of the present invention, and FIG. 7 is a schematic diagram showing a conventional ventilation air conditioning system. 1... Reactor building 2... Central control room 3a,
3b...Blower 20...Carbon dioxide removal device 21...Blow pipe 22...Removal tank 23...Bubbling device 24...Exhaust pipe 25.
...Water pipe 26...Drainage pipe agent Patent attorney Noriyuki Chika (and 1 other person) (a)
tb-Figure 2 Figure 3 Figure 4 Figure 5

Claims (3)

【特許請求の範囲】[Claims] (1)原子炉建屋内に設置された中央制御室の空気を換
気する換気空調設備において、前記中央制御室内の空気
を排風機により導びき出し、この空気を排風機の下流側
の管路に設けられた二酸化炭素を吸収する二酸化炭素除
去装置を通した後、再び前記中央制御室内に送出させて
成ることを特徴とする換気空調設備。
(1) In ventilation air conditioning equipment that ventilates the air in a central control room installed in a reactor building, the air in the central control room is drawn out by an exhaust fan, and this air is passed through a pipe downstream of the exhaust fan. A ventilation air conditioning system characterized in that the carbon dioxide is passed through a carbon dioxide removal device provided to absorb the carbon dioxide and then sent back into the central control room.
(2)前記二酸化炭素除去装置は、二酸化炭素を吸収す
る液体を保有する除去タンクと、この除去タンク内に中
央制御室内の空気を送入させる送風管と、この送風管の
先端に設けられかつ多数の孔が形成されたバブリング装
置と、二酸化炭素が除去された空気を除去タンク外へ排
出する排風管と、前記二酸化炭素を吸収する液体を除去
タンク内に注入する送水管と、この二酸化炭素を吸収す
る液体を除去タンク外へ排出する排出管とから成ること
を特徴とする特許請求の範囲第1項記載の換気空調設備
(2) The carbon dioxide removal device includes a removal tank that holds a liquid that absorbs carbon dioxide, a blow pipe that blows air from the central control room into the removal tank, and a carbon dioxide removal device that is provided at the tip of the blow pipe. A bubbling device with a large number of holes formed therein, an exhaust pipe for discharging the air from which carbon dioxide has been removed to the outside of the removal tank, a water pipe for injecting the liquid that absorbs the carbon dioxide into the removal tank, and a The ventilation air conditioning equipment according to claim 1, comprising a discharge pipe for discharging the carbon-absorbing liquid to the outside of the removal tank.
(3)前記二酸化炭素を吸収する液体は、石炭、水酸化
ナトリウム、水酸化バリウム、酸化バリウム及び酸化マ
グネシウムの少なくとも1部材が混入されて成ることを
特徴とする特許請求の範囲第2項記載の換気空調設備。
(3) The liquid that absorbs carbon dioxide is formed by mixing at least one of coal, sodium hydroxide, barium hydroxide, barium oxide, and magnesium oxide. Ventilation and air conditioning equipment.
JP60119803A 1985-06-04 1985-06-04 Ventilating and air-conditioning facility Pending JPS61280336A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60119803A JPS61280336A (en) 1985-06-04 1985-06-04 Ventilating and air-conditioning facility

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60119803A JPS61280336A (en) 1985-06-04 1985-06-04 Ventilating and air-conditioning facility

Publications (1)

Publication Number Publication Date
JPS61280336A true JPS61280336A (en) 1986-12-10

Family

ID=14770608

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60119803A Pending JPS61280336A (en) 1985-06-04 1985-06-04 Ventilating and air-conditioning facility

Country Status (1)

Country Link
JP (1) JPS61280336A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007032909A (en) * 2005-07-26 2007-02-08 Shimizu Corp Air-conditioning system with decontaminating and carbon dioxide eliminating function
JP2011027308A (en) * 2009-07-24 2011-02-10 Hitachi-Ge Nuclear Energy Ltd Ventilation method of central control room and central control room ventilation device
JP2013108712A (en) * 2011-11-24 2013-06-06 Central Research Institute Of Electric Power Industry Thermo-hygrostat
JP2015007603A (en) * 2013-05-31 2015-01-15 三菱重工業株式会社 Ventilation system
JP2016527499A (en) * 2013-07-19 2016-09-08 アレヴァ ゲゼルシャフト ミット ベシュレンクテル ハフツングAreva GmbH Ventilation system for use in severe accidents in nuclear facilities and method of operation thereof
JP2018502303A (en) * 2015-01-16 2018-01-25 アレヴァ ゲゼルシャフト ミット ベシュレンクテル ハフツングAreva GmbH Ventilation system for use in severe accidents in nuclear facilities and method of operation thereof
JP2019109129A (en) * 2017-12-18 2019-07-04 株式会社東芝 Oxygen concentration control facility of building for nuclear power and oxygen concentration control method
CN110410918A (en) * 2019-07-12 2019-11-05 中国核电工程有限公司 The method and system that air output and air draft variable air rate operating condition match

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007032909A (en) * 2005-07-26 2007-02-08 Shimizu Corp Air-conditioning system with decontaminating and carbon dioxide eliminating function
JP2011027308A (en) * 2009-07-24 2011-02-10 Hitachi-Ge Nuclear Energy Ltd Ventilation method of central control room and central control room ventilation device
JP2013108712A (en) * 2011-11-24 2013-06-06 Central Research Institute Of Electric Power Industry Thermo-hygrostat
JP2015007603A (en) * 2013-05-31 2015-01-15 三菱重工業株式会社 Ventilation system
JP2016527499A (en) * 2013-07-19 2016-09-08 アレヴァ ゲゼルシャフト ミット ベシュレンクテル ハフツングAreva GmbH Ventilation system for use in severe accidents in nuclear facilities and method of operation thereof
JP2018502303A (en) * 2015-01-16 2018-01-25 アレヴァ ゲゼルシャフト ミット ベシュレンクテル ハフツングAreva GmbH Ventilation system for use in severe accidents in nuclear facilities and method of operation thereof
JP2019109129A (en) * 2017-12-18 2019-07-04 株式会社東芝 Oxygen concentration control facility of building for nuclear power and oxygen concentration control method
CN110410918A (en) * 2019-07-12 2019-11-05 中国核电工程有限公司 The method and system that air output and air draft variable air rate operating condition match

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