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JPH0452430B2 - - Google Patents
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JPH0452430B2 - - Google Patents

Info

Publication number
JPH0452430B2
JPH0452430B2 JP58078342A JP7834283A JPH0452430B2 JP H0452430 B2 JPH0452430 B2 JP H0452430B2 JP 58078342 A JP58078342 A JP 58078342A JP 7834283 A JP7834283 A JP 7834283A JP H0452430 B2 JPH0452430 B2 JP H0452430B2
Authority
JP
Japan
Prior art keywords
suppression chamber
pressure suppression
pool water
water
filtration
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
JP58078342A
Other languages
Japanese (ja)
Other versions
JPS59203992A (en
Inventor
Koichi Taira
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
Tokyo Shibaura Electric Co 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 Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP58078342A priority Critical patent/JPS59203992A/en
Publication of JPS59203992A publication Critical patent/JPS59203992A/en
Publication of JPH0452430B2 publication Critical patent/JPH0452430B2/ja
Granted 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

  • Structure Of Emergency Protection For Nuclear Reactors (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は圧力抑制室の清浄度維持装置に係り、
特に圧力抑制室のプール水の水質浄化および圧力
抑制室の内壁の除染性を向上させる圧力抑制室の
清浄度維持装置に関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to a cleanliness maintenance device for a pressure suppression chamber,
In particular, the present invention relates to a pressure suppression chamber cleanliness maintenance device that improves the quality of pool water in the pressure suppression chamber and the decontamination of the inner wall of the pressure suppression chamber.

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

一般に沸騰水型原子力発電所では圧力抑制室を
有する。この圧力抑制室は原子炉圧力容器および
原子炉格納容器内の高温高圧蒸気を流入させてこ
の蒸気を凝縮させる蒸気の凝縮槽からなり、非常
用炉心冷却系の水源ともなる。また一次系配管の
破断事故発生等の非常時には圧力抑制室に貯蔵さ
れるプール水は原子炉圧力容器へ注入され、その
炉心を再冠水させて冷却するために使用される。
この非常用炉心冷却系については原子炉の運転中
および停止中にこの冷却系の健全性確認試験が適
宜実施され、圧力抑制室への蒸気の出入が繰り返
えされる。また、原子炉起動・停止の操作中に原
子炉圧の過上昇があつた場合はやはり高圧蒸気が
圧力抑制室へ流入される。この流入する蒸気によ
り圧力抑制室へは多量の放射化した腐食生成物が
流入する。この腐食生成物は原子炉の運転年数に
伴ない年々増加し、長期間放置されて圧力抑制室
の底部等に堆積している。圧力抑制室の汚染はそ
のプール水を水源とする、例えば非常用炉心冷却
系等の各種機器の機能および健全性を害する恐れ
が発生する。そこで、プール水の浄化が望まれて
いた。また圧力抑制室の内壁の補修、再塗装等の
際はこの内壁の除染作業が事前に実施されるが、
内壁の汚染のために多大な労力と時間を要すると
共に、この除染作業に従事する作業員への放射線
被曝の低減、そして内壁の補修等工事期間短縮化
の見地から圧力抑制室の洗浄化が従来から強く望
まれていた。
Boiling water nuclear power plants generally have a pressure suppression chamber. This pressure suppression chamber consists of a steam condensing tank into which high-temperature, high-pressure steam in the reactor pressure vessel and reactor containment vessel flows and condenses the steam, and also serves as a water source for the emergency core cooling system. In addition, in the event of an emergency such as a rupture of the primary system piping, the pool water stored in the pressure suppression chamber is injected into the reactor pressure vessel and used to re-flood the reactor core and cool it.
Tests to confirm the integrity of this emergency core cooling system are conducted as appropriate during operation and shutdown of the reactor, and steam is repeatedly brought in and out of the pressure suppression chamber. Furthermore, if the reactor pressure rises excessively during reactor startup/shutdown operations, high-pressure steam also flows into the pressure suppression chamber. This inflowing steam causes a large amount of activated corrosion products to flow into the pressure suppression chamber. This corrosion product increases year by year as the reactor operates, and is deposited at the bottom of the pressure suppression chamber after being left unused for a long time. Contamination of the pressure suppression chamber may impair the function and integrity of various equipment that uses the pool water as a water source, such as the emergency core cooling system. Therefore, purification of pool water was desired. In addition, when the inner walls of the pressure suppression chamber are repaired or repainted, decontamination work is carried out in advance.
Contamination of the inner walls requires a great deal of labor and time, and the pressure suppression chamber must be cleaned in order to reduce radiation exposure to workers engaged in decontamination work and to shorten the construction period for repairing the inner walls. It has long been strongly desired.

〔発明の目的〕[Purpose of the invention]

本発明は上述した事情に鑑みなされたものであ
り、圧力抑制室のプール水の水質を浄化すると共
に、圧力抑制室を清浄化して原子炉系の信頼性お
よび健全性を向上し、圧力抑制室の除染作業の作
業能率を向上することができる圧力抑制室の清浄
度維持装置を提供することを目的とする。
The present invention was made in view of the above-mentioned circumstances, and it purifies the water quality of the pool water in the pressure suppression chamber, and also purifies the pressure suppression chamber to improve the reliability and soundness of the reactor system. An object of the present invention is to provide a cleanliness maintenance device for a pressure suppression chamber that can improve the efficiency of decontamination work.

〔発明の概要〕[Summary of the invention]

上記の目的を達成するため、本発明は次のよう
に構成される。
In order to achieve the above object, the present invention is configured as follows.

圧力抑制室を有する沸騰水型原子炉のものにお
いて、上記圧力抑制室の空間部とそのプール水中
とを連通する給気配管にブロアーを設けると共
に、この給気配管のプール水中に水没する水没部
に圧力抑制室の底部ほぼ全周に配設される吹出用
分岐管を接続し、この吹出用分岐管の管軸方向に
多数の吹出孔を圧力抑制室内底部に向けて形成
し、一方圧力抑制室のプール水をこの圧力抑制室
へ循環させる循環配管に、プール水強制循環用の
ポンプと、プール水の水質を浄化するろ過脱塩装
置とをそれぞれ設けて構成される。
In a boiling water reactor having a pressure suppression chamber, a blower is provided in the air supply piping that communicates the space of the pressure suppression chamber with the water in the pool, and a submerged portion of the air supply piping is submerged in the pool water. A branch pipe for blowing disposed around the entire bottom of the pressure suppression chamber is connected to the branch pipe for blowing out, and a large number of blowing holes are formed in the axial direction of the branch pipe for blowing toward the bottom of the pressure suppression chamber. The circulation piping that circulates the pool water in the chamber to the pressure suppression chamber is provided with a pump for forced circulation of the pool water and a filtration desalination device that purifies the quality of the pool water.

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

以下本発明に係る圧力抑制室の清浄度維持装置
の一実施例について図面を参照して説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a pressure suppression chamber cleanliness maintenance device according to the present invention will be described below with reference to the drawings.

第1図は沸騰水型原子炉マーク型に本発明を
適用した場合の構成を示す全体構成図であり、図
中符号1は図示しない原子炉建屋内に収容されて
いる原子炉格納容器である。この原子炉格納容器
1内には原子炉圧力容器2が収容され、この原子
炉圧力容器2の下方に圧力抑制室3が配置されて
いる。この圧力抑制室3内にはプール水4が貯蔵
され、このプール水4面上は空間部3aをおいて
ダイアフラムフロア5により仕切られている。こ
のダイヤフラムフロア5には上記原子炉格納器1
内へ流入した炉水等を圧力抑制室3内へ導くため
のベント管6が適宜数取付けられている。この圧
力抑制室3に清浄度維持装置を設けるのである
が、この清浄度維持装置は圧力抑制室3のプール
水4を撹拌する撹拌装置と、圧力抑制室3内のプ
ール水の水質を浄化する浄化装置とから主に構成
されている。撹拌装置としては例えば次のように
構成される。
FIG. 1 is an overall configuration diagram showing the configuration when the present invention is applied to a boiling water reactor mark type, and the reference numeral 1 in the figure is a reactor containment vessel housed in a reactor building (not shown). . A reactor pressure vessel 2 is housed within the reactor containment vessel 1, and a pressure suppression chamber 3 is arranged below the reactor pressure vessel 2. Pool water 4 is stored in this pressure suppression chamber 3, and the surface of this pool water 4 is partitioned off by a diaphragm floor 5 with a space 3a in between. This diaphragm floor 5 has the reactor containment 1
An appropriate number of vent pipes 6 are installed to guide reactor water and the like flowing into the pressure suppression chamber 3. This pressure suppression chamber 3 is provided with a cleanliness maintenance device, which includes a stirring device that stirs the pool water 4 in the pressure suppression chamber 3, and a stirring device that purifies the quality of the pool water in the pressure suppression chamber 3. It mainly consists of a purification device. The stirring device is configured as follows, for example.

まず圧力抑制室3のプール水4中とその空間部
3aとを連通する給気配管7を設ける。この給気
配管7の中間部は第1図に示すように原子炉格納
容器1の外側に配置され、ブロアー8を介装して
いる。一方、圧力抑制室のプール水4中に延出す
る給気配管7の水没端部は吹出用分岐配管9に多
数分岐し、これら吹出用分岐配管9は第2図に示
すようにその管軸方向に多数の吹出孔10が連設
されている。これら吹出用分岐配管9は圧力抑制
室3内の底部または底部近傍もしくは内側壁近傍
に配置され、環状の圧力抑制室3のほぼ全周に設
けられる。
First, an air supply pipe 7 is provided which communicates the pool water 4 of the pressure suppression chamber 3 with the space 3a thereof. As shown in FIG. 1, the intermediate portion of the air supply pipe 7 is disposed outside the reactor containment vessel 1, and a blower 8 is interposed therebetween. On the other hand, the submerged end of the air supply pipe 7 extending into the pool water 4 of the pressure suppression chamber branches into a number of branch pipes 9 for blowing out, and these branch pipes 9 for blowing out have their pipe axes as shown in FIG. A large number of blow-off holes 10 are arranged in a row in the direction. These blowout branch pipes 9 are arranged at the bottom of the pressure suppression chamber 3 or near the bottom or near the inner wall, and are provided around the entire circumference of the annular pressure suppression chamber 3.

さらに、吹出用分岐配管9に設けた吹出孔10
は圧力抑制室3内底部に向けて開口されると共
に、圧力抑制室3内側壁の近傍に配置される吹出
用分岐配管9については、その内側壁に向けて開
口され、圧力抑制室3内側壁に附着している腐食
生成物等の脱落を容易にするように構成されてい
る。
Further, a blowout hole 10 provided in the blowout branch pipe 9
is opened toward the inner bottom of the pressure suppression chamber 3, and the outlet branch pipe 9 disposed near the inner wall of the pressure suppression chamber 3 is opened toward the inner wall thereof, and is opened toward the inner bottom of the pressure suppression chamber 3. The structure is designed to facilitate the removal of corrosion products, etc. attached to the

一方、浄化装置としては例えば次のように構成
される。
On the other hand, the purifying device is configured as follows, for example.

圧力抑制室3にこの圧力抑制室3のプール水4
を循環させる循環配管11を設ける。この循環配
管11のプール水4吸込口は圧力抑制室3内の下
部に開口し、他方循環配管11の吐出口は上記吸
込口の上方に位置するように配置されている。こ
の循環配管11にはその吸込口から吐出口方向へ
循環用ポンプ12およびろ過脱塩装置13が順次
介装される。
The pool water 4 of this pressure suppression chamber 3 is transferred to the pressure suppression chamber 3.
A circulation pipe 11 is provided to circulate the water. The pool water 4 suction port of this circulation pipe 11 opens at the lower part of the pressure suppression chamber 3, and the discharge port of the circulation pipe 11 is arranged above the above-mentioned suction port. A circulation pump 12 and a filtration/desalination device 13 are sequentially installed in this circulation pipe 11 from its suction port to its discharge port.

次に上述した本発明の一実施例の作用について
述べる。
Next, the operation of the embodiment of the present invention described above will be described.

まずブロアー8を起動すると、圧力抑制室3の
空間部3aの気体、例えば窒素、空気等が吸入さ
れて給気配管7を介して吹出用分岐配管9へ供給
され、この吹出用分岐配管9の吹出孔10から圧
力抑制室3のプール水4中へ吹出される。この空
気等の気体がプール水4中に配設された吹出用分
岐配管9から吹出すと、圧力抑制室3の底部に沈
澱、堆積している腐食生成物がプール水4上方へ
上昇するような水流が生じ、プール水4面上に浮
遊している腐食生成物と共にプール水4は撹拌さ
れる。この撹拌時には圧力抑制室3の内壁に附着
した腐食生成物もプール水4中に脱落する。吹出
用分岐配管9は圧力抑制室3のほぼ全周に亘つて
配置されているので、上記プール水4の撹拌は圧
力抑制室3のほぼ全周で行なわれる。このような
プール水4の撹拌時に循環用ポンプ12が駆動さ
れると、循環配管11の吸込口よりプール水4が
吸込まれる。プール水4の吸込み時には上述した
ようにプール水4は既に撹拌されているので圧力
抑制室3の底部に沈澱、堆積し、その内壁に附着
した腐食生成物と共に吸込まれる。この吸込水は
循環用ポンプ2によりろ過脱塩装置13に送出さ
れ、このろ過脱塩装置13にて上記腐食生成物等
異物がろ過され、水質が浄化される。このろ過脱
塩装置13にて水質が浄化されたプール水4は循
環配管11の吐出口より圧力抑制室3内へ注入さ
れる。したがつて上記ブロアー7や循環ポンプ1
2等が所定時間運転されると、圧力抑制室3内底
部に沈澱、堆積され、また内壁に附着した腐食生
成物がろ過脱塩装置13にてろ過され、プール水
4の水質が浄化されると共に、圧力抑制室3内壁
が清浄化される。
First, when the blower 8 is started, gas such as nitrogen, air, etc. in the space 3a of the pressure suppression chamber 3 is sucked in and supplied to the blowout branch pipe 9 via the air supply pipe 7. It is blown out from the blow-off hole 10 into the pool water 4 of the pressure suppression chamber 3. When this gas such as air is blown out from the blowout branch pipe 9 disposed in the pool water 4, the corrosion products precipitated and deposited at the bottom of the pressure suppression chamber 3 rise upward to the pool water 4. A water flow is generated, and the pool water 4 is stirred together with the corrosion products floating on the surface of the pool water 4. During this stirring, corrosion products adhering to the inner wall of the pressure suppression chamber 3 also fall into the pool water 4. Since the blowout branch pipe 9 is disposed around almost the entire circumference of the pressure suppression chamber 3, the pool water 4 is stirred almost all around the pressure suppression chamber 3. When the circulation pump 12 is driven during such agitation of the pool water 4, the pool water 4 is sucked through the suction port of the circulation pipe 11. When the pool water 4 is being sucked in, the pool water 4 has already been stirred as described above, so it settles and accumulates at the bottom of the pressure suppression chamber 3, and is sucked in together with the corrosion products attached to the inner wall thereof. This suction water is sent to a filtration and demineralization device 13 by the circulation pump 2, where foreign substances such as the corrosion products are filtered out and the water quality is purified. The pool water 4 whose water quality has been purified by the filtration and demineralization device 13 is injected into the pressure suppression chamber 3 from the outlet of the circulation pipe 11. Therefore, the blower 7 and the circulation pump 1
When the second class is operated for a predetermined period of time, corrosion products that are precipitated and deposited on the inner bottom of the pressure suppression chamber 3 and attached to the inner wall are filtered by the filtration desalination device 13, and the quality of the pool water 4 is purified. At the same time, the inner wall of the pressure suppression chamber 3 is cleaned.

次に本発明に沸騰水型原子炉マーク型に適用
した場合の他の実施例について第3図に基づいて
説明する。
Next, another embodiment in which the present invention is applied to a boiling water reactor mark type will be described with reference to FIG.

沸騰水型原子炉マーク型では圧力抑制室20
が第3図に示すようにトーラス状の形状をなし、
原子炉格納容器1の下部外周に環状に配置されて
いる。また本実施例では浄化装置としての構成各
部、例えば循環ポンプ12は残留熱除去系の例え
ば炉水注入用の注入ポンプ21を、またろ過脱塩
装置13は復水浄化系のろ過脱塩装置22をそれ
ぞれ共用する構成となつている。本実施例では撹
拌装置としての構成は上述の第1実施例とほぼ同
一構成であるので、その説明は省略する。
In the boiling water reactor mark type, pressure suppression chamber 20
has a torus-like shape as shown in Figure 3,
They are arranged in a ring shape around the lower outer periphery of the reactor containment vessel 1. Further, in this embodiment, each component of the purification device, for example, the circulation pump 12 is a residual heat removal system, such as an injection pump 21 for injecting reactor water, and the filtration desalination device 13 is a filtration desalination device 22 of a condensate purification system. The configuration is such that they are shared by each. In this embodiment, the configuration of the stirring device is almost the same as that of the first embodiment described above, so the explanation thereof will be omitted.

上記残留熱除去系は原子炉運転停止後に原子炉
内の残留熱を除去するものであり、圧力抑制室2
0内のプール水4を原子炉内へ注入するための注
入ポンプ21を適宜数備えている。また復水浄化
系は復水の水質を浄化して原子炉へ供給するよう
にしたものであり、ろ過脱塩装置22を適宜数備
えている。そこで第3図に示すように、圧力抑制
室20のプール水4を吸込めるように注入ポンプ
21を設けた上記残留熱除去系の任意の吸込管2
3の中途に、上記注水ポンプ21の吐出側で入口
側接続管24をこの吸込管23から分岐するよう
に接続する。この入口側接続管24の他端は上述
の復水浄化系のろ過脱塩装置22の入口側に接続
される。ろ過脱塩装置22の出口側には出口側接
続管25を接続する。この出口側接続管25の他
端は残留熱除去系の戻し配管26の中途に接続さ
れて、1つの閉ループを形成し、圧力抑制室20
のプール水がこの閉ループを強制循環されるよう
になつている。そして上記入口側、出口側接続管
24,25に入口弁27、出口弁28をそれぞれ
設ける。また上記入口側接続管24および出口側
接続管25にそれぞれ接続された残留熱除去系お
よび復水浄化系の配管には、上記入口側、出口側
接続管24,25との接続箇所より上流側もしく
は下流側に止め弁29,30,31,32をそれ
ぞれ介装し、これら止め弁29,30,31,3
2を全て閉じたときに、注入ポンプ21により吸
込まれたプール水4が全てろ過脱塩装置22を流
通し、上記残留熱除去系および復水浄化系へは流
出しないように構成されている。
The residual heat removal system described above removes the residual heat inside the reactor after the reactor operation is stopped, and is installed in the pressure suppression chamber 2.
An appropriate number of injection pumps 21 are provided for injecting the pool water 4 in the reactor into the reactor. The condensate purification system purifies the water quality of condensate and supplies it to the nuclear reactor, and is equipped with an appropriate number of filtration and desalination devices 22. Accordingly, as shown in FIG.
3, an inlet side connecting pipe 24 is connected to the inlet side connecting pipe 24 so as to branch from this suction pipe 23 on the discharge side of the water injection pump 21. The other end of this inlet side connecting pipe 24 is connected to the inlet side of the filtration desalination device 22 of the above-mentioned condensate purification system. An outlet side connecting pipe 25 is connected to the outlet side of the filtration and demineralization device 22 . The other end of this outlet side connecting pipe 25 is connected to the middle of the return pipe 26 of the residual heat removal system to form one closed loop, and the pressure suppression chamber 20
pool water is forced to circulate through this closed loop. An inlet valve 27 and an outlet valve 28 are provided in the inlet and outlet connecting pipes 24 and 25, respectively. In addition, the piping of the residual heat removal system and the condensate purification system connected to the inlet side connecting pipe 24 and the outlet side connecting pipe 25, respectively, is provided on the upstream side from the connection point with the inlet side and outlet side connecting pipes 24, 25. Alternatively, stop valves 29, 30, 31, 32 are installed on the downstream side, and these stop valves 29, 30, 31, 3
2 are all closed, all of the pool water 4 sucked in by the injection pump 21 flows through the filtration desalination device 22, and is configured so as not to flow out to the residual heat removal system and condensate purification system.

すなわち、圧力抑制室20と注入ポンプ21と
ろ過脱塩装置22とこれらを互いに接続する配管
類により1つの閉ループが構成され、この注入ポ
ンプ21にて吸込まれた圧力抑制室20のプール
水4はこの閉ループを循環されるようになつてい
る。
That is, the pressure suppression chamber 20, the injection pump 21, the filtration desalination device 22, and the piping that connects these to each other constitute one closed loop, and the pool water 4 in the pressure suppression chamber 20 sucked by the injection pump 21 is It is designed to circulate in this closed loop.

したがつて撹拌装置側のブロアー8が起動され
ると、上述した第1実施例と同様にして圧力抑制
室20の空間部3aに流入した空気等の気体が給
気配管7を介してプール水4中に配置された吹出
用分岐配管9に供給される。この空気等の気体は
さらに吹出用分岐配管9の吹出孔10からプール
水4中へ吹出され、このプール水4を撹拌し、圧
力抑制室20内底部に沈澱、堆積し、または圧力
抑制室20内壁に附着した腐食生成物をプール水
4中へ舞い上げ水流を発生させ撹拌する。これと
同時に浄化装置側の注入ポンプ21を起動する
と、この注入ポンプ21は撹拌されているプール
水4を腐食生成物と共に吸込み、この吸込水をろ
過脱塩装置22へ輸送する。この際残留熱除去系
および復水浄化系に設けた止め弁29,30,3
1,32は全て閉じており、入口側、出口側接続
管24,25の入口弁27と出口弁28は開弁さ
れている。したがつて上述の吸込水は全てろ過脱
塩装置22へ流入し、ここでろ過脱塩処理されて
腐食生成物等の異物は除去され、水質が浄化され
てろ過脱塩装置22から吐出される。水質が浄化
された清浄水は戻し配管26を介して再び圧力抑
制室20内へ還入される。その結果、圧力抑制室
20内は清浄に維持されるようになる。
Therefore, when the blower 8 on the stirring device side is started, gas such as air that has flowed into the space 3a of the pressure suppression chamber 20 in the same manner as in the first embodiment described above flows through the air supply pipe 7 to the pool water. The air is supplied to a branch pipe 9 for blowing disposed in the pipe 4. This gas such as air is further blown out into the pool water 4 from the blow-off hole 10 of the blow-off branch pipe 9, stirs the pool water 4, and settles and accumulates on the inner bottom of the pressure suppression chamber 20, or Corrosion products adhering to the inner wall are blown up into the pool water 4 to generate a water flow and stir it. At the same time, when the injection pump 21 on the purification device side is started, the injection pump 21 sucks the pool water 4 being stirred together with the corrosion products and transports this suction water to the filtration and demineralization device 22 . At this time, stop valves 29, 30, 3 installed in the residual heat removal system and condensate purification system
1 and 32 are all closed, and the inlet valve 27 and outlet valve 28 of the inlet and outlet side connecting pipes 24 and 25 are open. Therefore, all of the above-mentioned suction water flows into the filtration and demineralization device 22, where it is subjected to filtration and demineralization treatment to remove foreign substances such as corrosion products, purify the water quality, and discharge it from the filtration and demineralization device 22. . The purified water is returned to the pressure suppression chamber 20 via the return pipe 26. As a result, the inside of the pressure suppression chamber 20 is maintained clean.

なお第3図中第1図と同一または相当部分には
同一符号を付してその説明を省略している。
Note that the same or equivalent parts in FIG. 3 as in FIG. 1 are given the same reference numerals and their explanations are omitted.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明は、圧力抑制室内の
プール水を撹拌すると共に、このプール水を浄化
し、同時に圧力抑制室を清浄にするように構成し
たので、この圧力抑制室内での腐食生成物の堆
積、附着を防止し、プール水の清浄度を常に維持
することができる。その結果流体設備としての原
子炉系諸設備、諸機器の健全性およびその信頼性
を向上することができる。しかも、残留熱除去系
のポンプや復水浄化系のろ過脱塩装置等を共用す
ることができるので、低コストで上述の効果を奏
することができる。また圧力抑制室を常時清浄に
維持することができるので、再塗装作業等に伴う
圧力抑制室内の除染性を向上することができると
共に、その作業時間の短縮、その作業時に作業員
が被曝する放射線の低減をはかるこができる。さ
らにプール水中に放出する気体を圧力抑制室内の
気体としたので放射性気体廃棄物の量を最少限に
することができる。また、吹出用分岐管は圧力抑
制室の底部ほぼ全周に配設されかつ吹出孔を底部
に向けているので少量の放出気体で効率よくプー
ル全体を撹拌することができる。さらに吹出孔が
底部に向けられているので腐食生成物が吹出孔内
に堆積し、閉塞することができる。
As explained above, the present invention is configured to agitate the pool water in the pressure suppression chamber, purify the pool water, and simultaneously clean the pressure suppression chamber, so that corrosion products in the pressure suppression chamber are removed. The cleanliness of pool water can be maintained at all times by preventing the accumulation and adhesion of water. As a result, the health and reliability of nuclear reactor system equipment and equipment as fluid equipment can be improved. Furthermore, since the pump for the residual heat removal system, the filtration desalination device for the condensate purification system, etc. can be shared, the above-mentioned effects can be achieved at low cost. In addition, since the pressure suppression chamber can be kept clean at all times, it is possible to improve the decontamination of the pressure suppression chamber during repainting work, etc., reduce work time, and reduce worker exposure to radiation during the work. Radiation can be reduced. Furthermore, since the gas released into the pool water is the gas in the pressure suppression chamber, the amount of radioactive gas waste can be minimized. Further, since the blowout branch pipe is disposed around the entire bottom of the pressure suppression chamber and the blowout hole is directed toward the bottom, the entire pool can be efficiently agitated with a small amount of released gas. Furthermore, since the blow-off holes are directed toward the bottom, corrosion products can accumulate in the blow-off holes and block them.

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

第1図は本発明の一実施例の構成を説明するた
めの全体構成図、第2図は同、吹出用分岐配管の
一部分の拡大斜視図、第3図は同、他の実施例の
全体構成図である。 1……原子炉格納容器、2……原子炉圧力容
器、3,20……圧力抑制室、4……プール水、
7……給気配管、8……ブロアー、9……吹出用
分岐配管、10……吹出孔、11……循環配管、
12……循環ポンプ、13,22……ろ過脱塩装
置、21……注入ポンプ、24……入口側接続
管、25……出口側接続管、29,30,31,
32……止め弁。
Fig. 1 is an overall configuration diagram for explaining the configuration of one embodiment of the present invention, Fig. 2 is an enlarged perspective view of a part of the branch pipe for blowing out the same, and Fig. 3 is the whole of another embodiment of the same. FIG. 1... Reactor containment vessel, 2... Reactor pressure vessel, 3, 20... Pressure suppression chamber, 4... Pool water,
7...Air supply piping, 8...Blower, 9...Blowout branch pipe, 10...Blowout hole, 11...Circulation pipe,
12... Circulation pump, 13, 22... Filtration desalination device, 21... Injection pump, 24... Inlet side connection pipe, 25... Outlet side connection pipe, 29, 30, 31,
32...stop valve.

Claims (1)

【特許請求の範囲】 1 圧力抑制室を備えた沸騰水型原子炉のものに
おいて、上記圧力抑制室の空間部とそのプール水
中とを連通する給気配管にブロアーを設けると共
に、この給気配管のプール水中に水没する水没部
に圧力抑制室の底部ほぼ全周に配設される吹出用
分岐管を接続し、この吹出用分岐管の管軸方向に
多数の吹出孔を圧力抑制室内底部に向けて形成
し、一方圧力抑制室のプール水をこの圧力抑制室
へ循環させる循環配管に、プール水強制循環用の
ポンプと、プール水の水質を浄化するろ過脱塩装
置とをそれぞれ設けたことを特徴とする圧力抑制
室の清浄度維持装置。 2 プール水強制循環用ポンプは残留熱除去系の
プール水輸送用のポンプを共用したことを特徴と
する特許請求の範囲第1項記載に記載の圧力抑制
室の清浄度維持装置。 3 ろ過脱塩装置は復水浄化系のろ過脱塩装置を
共用したことを特徴とする特許請求の範囲第1項
に記載の圧力抑制室の清浄度維持装置。
[Scope of Claims] 1. In a boiling water reactor equipped with a pressure suppression chamber, a blower is provided in the air supply piping that communicates the space of the pressure suppression chamber with the pool water, and the air supply piping is provided with a blower. A branch pipe for blowing out that is arranged around the entire bottom of the pressure suppression chamber is connected to the submerged part of the pool that is submerged in water, and a large number of blowing holes are installed in the axial direction of the branch pipe for blowing out at the bottom of the pressure suppression chamber. On the other hand, a pump for forced circulation of pool water and a filtration desalination device for purifying the quality of pool water are installed in the circulation piping that circulates pool water from the pressure suppression chamber to this pressure suppression chamber. A pressure suppression chamber cleanliness maintenance device characterized by: 2. The cleanliness maintenance device for a pressure suppression chamber according to claim 1, wherein the pump for forced circulation of pool water is a pump for transporting pool water of a residual heat removal system. 3. The cleanliness maintenance device for a pressure suppression chamber according to claim 1, wherein the filtration and desalination device is a filtration and desalination device of a condensate purification system.
JP58078342A 1983-05-06 1983-05-06 Cleanness maintenance device for pressure suppression chamber Granted JPS59203992A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58078342A JPS59203992A (en) 1983-05-06 1983-05-06 Cleanness maintenance device for pressure suppression chamber

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58078342A JPS59203992A (en) 1983-05-06 1983-05-06 Cleanness maintenance device for pressure suppression chamber

Publications (2)

Publication Number Publication Date
JPS59203992A JPS59203992A (en) 1984-11-19
JPH0452430B2 true JPH0452430B2 (en) 1992-08-21

Family

ID=13659307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58078342A Granted JPS59203992A (en) 1983-05-06 1983-05-06 Cleanness maintenance device for pressure suppression chamber

Country Status (1)

Country Link
JP (1) JPS59203992A (en)

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5410886A (en) * 1977-06-27 1979-01-26 Toshiba Corp Reactor contrainer
JPS56144400U (en) * 1980-03-31 1981-10-30
JPS57168094U (en) * 1981-04-17 1982-10-22
JPS5828698A (en) * 1981-08-14 1983-02-19 株式会社東芝 Device for cooling and cleaning fuel pool water and pressure suppression pool water

Also Published As

Publication number Publication date
JPS59203992A (en) 1984-11-19

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