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JPH0679073B2 - Reactor coolant purification system - Google Patents
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JPH0679073B2 - Reactor coolant purification system - Google Patents

Reactor coolant purification system

Info

Publication number
JPH0679073B2
JPH0679073B2 JP61060075A JP6007586A JPH0679073B2 JP H0679073 B2 JPH0679073 B2 JP H0679073B2 JP 61060075 A JP61060075 A JP 61060075A JP 6007586 A JP6007586 A JP 6007586A JP H0679073 B2 JPH0679073 B2 JP H0679073B2
Authority
JP
Japan
Prior art keywords
reactor
pump
purification system
heat exchanger
purification
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
JP61060075A
Other languages
Japanese (ja)
Other versions
JPS62215894A (en
Inventor
公文 円谷
実 秋田
忠 白石
詳一郎 木下
稔 大倉
昭夫 辻
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 Ltd
Hitachi Industry and Control Solutions Co Ltd
Original Assignee
Hitachi Engineering Co Ltd Ibaraki
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 Engineering Co Ltd Ibaraki, Hitachi Ltd filed Critical Hitachi Engineering Co Ltd Ibaraki
Priority to JP61060075A priority Critical patent/JPH0679073B2/en
Publication of JPS62215894A publication Critical patent/JPS62215894A/en
Publication of JPH0679073B2 publication Critical patent/JPH0679073B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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】 〔産業上の利用分野〕 本発明は、原子炉冷却材浄化系に係り、特に、ポンプの
放射能汚染を低減した構成の原子炉冷却材浄化系に関す
る。
The present invention relates to a reactor coolant purification system, and more particularly to a reactor coolant purification system configured to reduce radioactive contamination of a pump.

〔従来の技術〕[Conventional technology]

従来の沸騰水型原子炉(以下、BWRという)の系統構成
の一例の概略を第6図に示す。BWRは、再循環系,給水
系,残留熱除去系,および本発明の対象である原子炉冷
却材浄化系などを備えている。
Fig. 6 shows an outline of an example of the system configuration of a conventional boiling water reactor (hereinafter referred to as BWR). The BWR includes a recirculation system, a water supply system, a residual heat removal system, and a reactor coolant purification system which is the subject of the present invention.

このうち、再循環系は、再循環ポンプ2(以下、PLRポ
ンプという)で昇圧した炉水を原子炉圧力容器1内に戻
して炉水を強制循環させる系統である。
Among them, the recirculation system is a system for returning the reactor water whose pressure is increased by the recirculation pump 2 (hereinafter referred to as a PLR pump) into the reactor pressure vessel 1 and forcibly circulating the reactor water.

給水系は、圧力容器1で生じた蒸気にタービン9で仕事
をさせた後、主復水器10で凝縮させ復水として、復水を
圧力容器1に戻す系統である。
The water supply system is a system in which steam generated in the pressure vessel 1 is caused to work in the turbine 9 and then condensed in the main condenser 10 to be condensed water to return the condensed water to the pressure vessel 1.

原子炉停止時の原子炉冷却は、主復水器10および残留熱
除去系で行われる。すなわち、原子炉冷却は、原子炉が
通常運転圧力(約70kg/cm2g)からタービングランドシ
ールが効かなくなる圧力(約9.0kg/cm2g)に下がるま
では主復水器10により行われ、それ以降の低圧時には残
留熱除去系により行われる。
Cooling of the reactor when the reactor is stopped is performed by the main condenser 10 and the residual heat removal system. In other words, reactor cooling is performed by the main condenser 10 until the reactor pressure decreases from the normal operating pressure (about 70 kg / cm 2 g) to the pressure at which the turbine gland seal does not work (about 9.0 kg / cm 2 g). At a low pressure thereafter, it is performed by the residual heat removal system.

残留熱除去系は、原子炉停止時の低圧時には常時運転し
て再循環ポンプ2の吸込配管側から残留熱除去ポンプ3
(以下、RHRポンプという)で炉水を取出し、残留熱除
去系熱交換器4で原子炉補機冷却系により冷却した後
に、PLRポンプ2の吐出配管を経て圧力容器1に戻す閉
ループを構成して、原子炉の冷却を行う系統である。
The residual heat removal system is always operated at a low pressure when the reactor is shut down, and the residual heat removal pump 3 is operated from the suction pipe side of the recirculation pump 2.
(Hereinafter referred to as "RHR pump") takes out reactor water, cools it with the residual heat removal system heat exchanger 4 by the reactor auxiliary cooling system, and then forms a closed loop for returning to the pressure vessel 1 through the discharge pipe of the PLR pump 2. It is a system for cooling the reactor.

原子炉冷却材浄化系は、原子炉圧力容器1内が原子炉通
常運転時の高圧時(約70.0kg/cm2g)から原子炉停止時
の低圧時(〜0kg/cm2g)までの広範囲にわたって常時
運転し、炉水を浄化する系統である。原子炉冷却材浄化
系は、PLRポンプ2の吸込配管側から原子炉冷却材浄化
系ポンプ5(以下、CUWポンプという)により炉水を取
出し昇圧して、再生熱交換器6および非再生熱交換器7
で所定の温度(約50℃)まで冷却した後、浄化装置(ろ
過脱塩装置)8で炉水を浄化し、前記再生熱交換器6で
加温し、給水系を経て再び圧圧容器1へ戻す系統であ
る。
The reactor coolant purification system is designed to operate the reactor pressure vessel 1 from high pressure during normal reactor operation (approximately 70.0 kg / cm 2 g) to low pressure during reactor shutdown (up to 0 kg / cm 2 g). It is a system that constantly operates over a wide range to purify reactor water. The reactor coolant purification system takes out reactor water from the suction piping side of the PLR pump 2 by the reactor coolant purification system pump 5 (hereinafter referred to as CUW pump), pressurizes it, and regenerates heat exchanger 6 and non-regeneration heat exchange. Bowl 7
After cooling to a predetermined temperature (about 50 ° C) with, the reactor water is purified with a purification device (filtration desalination device) 8, heated with the regenerative heat exchanger 6, and returned to the pressure vessel 1 via the water supply system. It is a system to return.

これら系統の改善に関連するものとしては、特開昭55−
6260号,特開昭54−38498号などがある。
As for those related to the improvement of these systems, JP-A-55-
6260 and JP-A-54-38498.

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

特開昭55−6260号公報の例は、熱交換器,ポンプ,浄化
装置および同装置のバイパスラインから構成され、プラ
ント通常運転時には、ポンプが小流量で運転され、熱交
換器,ポンプ,浄化装置を経て原子炉圧力容器に炉水を
戻し、冷却材浄化装置として使用している。プラント停
止時には、ポンプが大流量で運転され、熱交換器,ポン
プ,浄化装置バイパスラインを経て原子炉圧力容器に炉
水を戻し、残留熱除去装置として使用する。
The example of JP-A-55-6260 is composed of a heat exchanger, a pump, a purifying device and a bypass line of the device. During normal plant operation, the pump is operated at a small flow rate and the heat exchanger, pump and purifying device are used. The reactor water is returned to the reactor pressure vessel through the device and used as a coolant purification device. When the plant is stopped, the pump is operated at a large flow rate, and the reactor water is returned to the reactor pressure vessel via the heat exchanger, the pump, and the purifier bypass line, and used as a residual heat removal device.

したがつて、この例は、プラントの運転状態によつて、
同一装置を、通常運転時は冷却材浄化装置に、停止時は
残留熱除去装置に切り換え使用することになる。ここ
で、前記BWRでの原子炉冷却材浄化系の容量は、一般に
残留熱除去系の容量の約1/15と小流量であるため、この
例で冷却材浄化装置として使用する場合は、配管および
機器内の流速が極端に遅くなり、配管および機器が放射
能汚染されることが考えられる。
Therefore, in this example, depending on the operating condition of the plant,
The same device will be used by switching to the coolant purifying device during normal operation and to the residual heat removing device when stopped. Here, the capacity of the reactor coolant purification system in the BWR is generally about 1/15 of the capacity of the residual heat removal system, which is a small flow rate. It is also possible that the flow velocity in the equipment becomes extremely slow and the piping and equipment are radioactively contaminated.

また、残留熱除去装置としては低圧時のみ使用される
が、冷却材浄化装置として通常運転時には高圧(約70kg
/cm2g)使用となるため、装置全体を高圧時の使用に耐
えるようにしておくことが不可欠であつた。
The residual heat removal device is used only at low pressure, but it is used as a coolant purification device at high pressure (about 70 kg
/ cm 2 g), it is essential to make the entire device durable to use under high pressure.

一方、特開昭54−38498号公報に示されているように、C
UWポンプを熱交換器の下流側でろ過脱塩装置の上流側に
設置し、ポンプ内流体の温度を低温化することでポンプ
内面に発生する酸化被膜を少なくし、これにより酸化被
膜中に吸収されるコバルト60の量を低減させ、定期検査
時の作業員の被ばく量を抑えることが考えられている。
On the other hand, as disclosed in JP-A-54-38498, C
The UW pump is installed on the downstream side of the heat exchanger and on the upstream side of the filter desalting device, and the temperature of the fluid inside the pump is lowered to reduce the oxide film generated on the inner surface of the pump, which absorbs it in the oxide film. It is considered to reduce the amount of cobalt 60 that is generated and to reduce the exposure dose of workers during regular inspections.

しかしながら第7図に示す様に浄化装置3の出口側(F
部)に比べて、入口側(E部)は約10倍も放射線量が高
く、CUWポンプの汚染を完全になくすることはできてい
ない。CUWポンプの汚染を完全になくするには、ポンプ
をろ過脱塩装置の下流側に設置すれば良いが、ポンプ移
設により、ポンプ入口側の圧力損失が増大し、従来の設
計ではポンプ入口側の押込み圧力不足となつてしまうか
ら、そのようにできなかつた。
However, as shown in FIG. 7, the outlet side (F
The radiation dose on the inlet side (E section) is about 10 times higher than on the other side, and it is not possible to completely eliminate the contamination of the CUW pump. To completely eliminate the contamination of the CUW pump, it is sufficient to install the pump on the downstream side of the filter desalination device.However, the pump transfer increases the pressure loss on the pump inlet side. I couldn't do that because I had insufficient pushing pressure.

なお、第7図において、A〜Fの各部は、第6図に示し
た位置を表わしている。すなわち、A部はCUWポンプの
出口側、B部は再生熱交換器、C部はその出口側、D部
は非再生熱交換器、E部が浄化装置入口側、F部は浄化
装置出口側である。
In addition, in FIG. 7, each part of A to F represents the position shown in FIG. That is, part A is the outlet side of the CUW pump, part B is the regenerative heat exchanger, part C is its outlet side, part D is the non-regenerative heat exchanger, part E is the purification device inlet side, and part F is the purification device outlet side. Is.

本発明の目的は、CUWポンプの入口側の押込み圧力を充
分に確保しながらCUWポンプの放射能汚染をなくした原
子炉冷却材浄化系を提供することである。
An object of the present invention is to provide a reactor coolant purification system that eliminates radioactive contamination of the CUW pump while sufficiently securing the pushing pressure on the inlet side of the CUW pump.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、上記目的を達成するために、浄化系のCUWポ
ンプをろ過脱塩装置の下流側に設置し、そのために不足
するポンプ入口側の押込み圧力を補うように、浄化系へ
の炉水取入れ口を残留熱除去系のRHRポンプ及び熱交換
器の下流側からとした系統構成を提案するものである。
In order to achieve the above-mentioned object, the present invention installs a CUW pump of a purification system on the downstream side of a filter desalination apparatus, so as to make up the pumping pressure on the pump inlet side that is insufficient for that purpose, the reactor water to the purification system is supplemented. We propose a system configuration where the intake port is from the downstream side of the RHR pump and heat exchanger of the residual heat removal system.

浄化系への炉水取入れ口は、再循環系のPLRポンプの下
流側としてもよい。
The reactor water intake to the purification system may be on the downstream side of the PLR pump of the recirculation system.

〔作用〕[Action]

原子炉冷却材浄化系は、原子炉通常運転時および停止時
を通して常時運転されているが、停止時には燃料棒から
のクラツドのはく離等により機器の放射能汚染の恐れが
あるから、プラント定期検査時の作業員の被ばく低減の
点で、特に、原子炉停止時に原子炉浄化設備を運転する
ことが重要である。
The reactor coolant purification system is always operated during normal reactor operation and during shutdown, but during shutdown, there is a risk of radioactive contamination of equipment due to flaking of cladding from fuel rods, etc. From the viewpoint of reducing the exposure of workers, it is particularly important to operate the reactor cleaning equipment when the reactor is shut down.

原子炉を停止した低圧時には、原子炉の崩壊熱,残留熱
を除去するためにRHRポンプと熱交換器を含む残留熱除
去系が常時運転しているが、従来の残留熱除去系は冷却
機能のみであつた。残留熱除去系を原子炉冷却材浄化系
の浄化装置と接続すれば、残留熱除去系がいわば冷却機
構と浄化機能の両方を有することとなり、原子炉停止時
に原子炉浄化系の浄化装置以外の部分の運転が不要とな
る。
At low pressure when the reactor is shut down, the residual heat removal system including the RHR pump and heat exchanger is always operating to remove decay heat and residual heat of the reactor, but the conventional residual heat removal system has a cooling function. It was only for me. If the residual heat removal system is connected to the purification device of the reactor coolant purification system, the residual heat removal system will have both a so-called cooling mechanism and a purification function. Partial operation is unnecessary.

ここで、従来の原子炉冷却材浄化系のCUWポンプ,熱交
換器,浄化装置の配置は、原子炉停止時にポンプの押込
み圧力あるいは有効ポンプ吸込みヘツド(以下、NPSHと
いう)が不足し、ポンプ内でキヤビテーシヨンンが発生
しポンプを損傷する恐れがあつたため、原子炉圧力容器
から炉水を取出した直後にCUWポンプを配置してポンプN
PSH不足を防止していた。しかし上記のように残留熱除
去系から浄化系のNPS不足分を補えば、前記原子炉停止
時のCUWポンプNPSH不足の問題が解決されるので、原子
炉浄化系の配置を熱交換器,浄化装置,ポンプの順にで
きる。このため、CUWポンプは浄化装置で浄化された炉
水を扱うことになり、ポンプの放射能汚染を低減でき
る。
Here, the conventional arrangement of the CUW pump, heat exchanger, and purification device for the reactor coolant purification system is because the pump pressure or effective pump suction head (hereinafter referred to as NPSH) is insufficient when the reactor is shut down. The CUW pump is placed immediately after the reactor water is taken out from the reactor pressure vessel, as it may cause pump damage and damage the pump.
It was preventing PSH shortage. However, if the NPS deficiency of the purification system is supplemented from the residual heat removal system as described above, the problem of the CUW pump NPSH deficiency at the time of reactor shutdown can be solved. It can be done in the order of equipment and pump. For this reason, the CUW pump handles reactor water purified by the purification device, and radioactive contamination of the pump can be reduced.

また、同様にNPSHの不足を原子炉冷却材再循環ポンプ吐
出圧力によつて補うこともでき、同様の効果が期待され
る。
Similarly, the shortage of NPSH can be compensated by the discharge pressure of the reactor coolant recirculation pump, and the same effect is expected.

〔実施例〕〔Example〕

本発明による原子炉冷却系浄化系の一実施例を第1図に
示す。本実施例は、熱交換器6,7,浄化装置8,CUWポンプ
5の順で配置した浄化系の浄化装置8の上流側に、残留
熱除去系の熱交換器4の下流配管から炉水取入れ用の配
管20を設け、浄化装置8の下流側配管から原子炉圧力容
器1に戻る配管21を接続し、切換え弁23,24,25などを配
置したものである。
FIG. 1 shows an embodiment of the reactor cooling system purification system according to the present invention. In this embodiment, the heat exchangers 6, 7, the purifying device 8, and the CUW pump 5 are arranged in this order on the upstream side of the purifying device 8 of the purifying system, from the downstream pipe of the heat exchanger 4 of the residual heat removing system to the reactor water. A pipe 20 for intake is provided, a pipe 21 returning from the downstream pipe of the purification device 8 to the reactor pressure vessel 1 is connected, and switching valves 23, 24, 25 and the like are arranged.

原子炉通常運転時の炉水の浄化は、圧力容器1から炉水
を取出し、原子炉冷却材浄化系熱交換器6,7で冷却して
浄化装置8で浄化し、CUWポンプ5で昇圧し、原子炉浄
化系熱交換器6にて加温し再び圧力容器1に戻すように
してなされる。
To purify the reactor water during normal reactor operation, take the reactor water out of the pressure vessel 1, cool it with the reactor coolant purification system heat exchangers 6, 7, purify it with the purification device 8, and pressurize it with the CUW pump 5. The heating is performed in the reactor cleaning system heat exchanger 6 and then returned to the pressure vessel 1 again.

原子炉停止時には、残留熱除去系が従来と同様に運転さ
れて原子炉を冷却する。炉水の浄化は、残留熱除去系の
RHRポンプ3と熱交換器4で昇圧冷却された炉水の一部
を、接続配管20により浄化装置8に導き浄化し、戻り配
管21で圧力容器1内に戻すようになつている。したがつ
て、本実施例では原子炉通常運転時には従来と同様に炉
水の浄化ができ、原子炉停止時には原子炉冷却材浄化系
のポンプなどは運転せずに残留熱除去系のみを運転する
だけで、冷却機能と浄化機能の両方が得られる。
When the reactor is shut down, the residual heat removal system operates in the same manner as in the past to cool the reactor. Purification of reactor water is performed by the residual heat removal system.
A part of the reactor water whose pressure is increased and cooled by the RHR pump 3 and the heat exchanger 4 is introduced into the purification device 8 by the connection pipe 20 and purified, and is returned into the pressure vessel 1 by the return pipe 21. Therefore, in this embodiment, during normal reactor operation, the reactor water can be purified as in the conventional case, and when the reactor is stopped, only the residual heat removal system is operated without operating the reactor coolant purification system pump and the like. By itself, both cooling function and purification function can be obtained.

既に述べたように、従来の原子炉冷却材浄化系では、CU
Wポンプを浄化装置下流側に配置した場合、原子炉通常
運転時は、圧力容器1内で高圧(約70.0kg/cm2g)であ
り、ポンプ5吸込側に充分な押込み圧力が得られるため
ポンプ5のNPSH上の問題はなかつた。しかし、原子炉が
停止した低圧時には、ポンプ5上流側の熱交換器6,7,浄
化装置8でその圧力損失によりCUWポンプ5に必要な押
込み圧力が不足してしまい、ポンプ5でキヤビテーシヨ
ンが発生する恐れがあり、ポンプ5のNPSH不足の問題が
あつた。そこで、従来の原子炉浄化設備は、CUWポンプ
5のNPSHを確保するために第6図に示すように、ポンプ
5,熱交換器6,7,浄化装置8の順に機器を配置している。
As already mentioned, in the conventional reactor coolant purification system, CU
When the W pump is placed on the downstream side of the purifier, the pressure is high (about 70.0 kg / cm 2 g) in the pressure vessel 1 during normal reactor operation, and sufficient pushing pressure can be obtained on the suction side of the pump 5. There was no problem with NPSH of Pump 5. However, when the reactor is at a low pressure, the pressure loss required by the CUW pump 5 is insufficient due to the pressure loss in the heat exchangers 6, 7 and the purification device 8 on the upstream side of the pump 5, and the pump 5 causes cavitation. There was a problem of lack of NPSH of pump 5. Therefore, in order to secure the NPSH of the CUW pump 5, the conventional reactor cleaning equipment is designed as shown in FIG.
5, the heat exchangers 6, 7 and the purification device 8 are arranged in this order.

これに対し、本実施例では、原子炉が停止した低圧時に
は、残留熱除去系のポンプ圧力を利用して炉水を浄化す
るので、ポンプ5のNPSH不足の問題が解決され、第1図
に示すように、熱交換器6,7,浄化装置8,ポンプ5の順に
機器を配置できる。この結果、ポンプ5は、原子炉圧力
容器1から取出された炉水を直接扱うことがなくなり、
CUWポンプ5の放射能汚染が低減される。
On the other hand, in the present embodiment, when the reactor is at a low pressure, the pump pressure of the residual heat removal system is used to purify the reactor water, so that the problem of NPSH shortage of the pump 5 is solved. As shown, the heat exchangers 6, 7, the purifier 8, and the pump 5 can be arranged in this order. As a result, the pump 5 does not directly handle the reactor water taken out from the reactor pressure vessel 1,
The radioactive contamination of the CUW pump 5 is reduced.

従来の原子炉冷却材浄化系の配管表面線量率の概略を示
す第7図によれば、浄化装置8下流側(F部)は、再生
熱交換器6上流側(A部)に比べて約1/100程度である
ことが解る。本実施例では、浄化装置8下流側配置によ
り、ポンプ5の放射能汚染を約1/100に低減可能であ
る。
According to FIG. 7 which shows the outline of the pipe surface dose rate of the conventional reactor coolant purification system, the downstream side of the purification device 8 (F section) is about 10% smaller than the upstream side of the regenerative heat exchanger 6 (A section). It turns out that it is about 1/100. In the present embodiment, the radioactive contamination of the pump 5 can be reduced to about 1/100 by disposing the purification device 8 on the downstream side.

また、原子炉停止時に原子炉冷却材浄化系ポンプ5熱交
換器6,7を停止できるため、弁23,24,25を閉じてこれら
を隔離し、機器を容易に点検できる。
Further, since the reactor coolant purification system pump 5 heat exchangers 6 and 7 can be stopped when the reactor is stopped, the valves 23, 24 and 25 can be closed to isolate them and the equipment can be easily inspected.

本発明の他の実施例を第2図,第3図に示す。Another embodiment of the present invention is shown in FIGS.

第2図は、残留熱除去系熱交換器4からの接続配管20を
原子炉冷却材浄化系再生熱交換器6の上流側に接続した
ものである。原子炉停止時に熱交換器6,7を通るので、
冷却機能が向上する。
FIG. 2 shows the connection pipe 20 from the residual heat removal system heat exchanger 4 connected to the upstream side of the reactor coolant purification system regenerative heat exchanger 6. Since it passes through the heat exchangers 6 and 7 when the reactor is shut down,
The cooling function is improved.

第3図は、2系統の残留熱除去系熱交換器4からの接続
配管20を原子炉冷却材浄化系に接続したものである。
FIG. 3 shows the connection pipe 20 from the two-system residual heat removal system heat exchanger 4 connected to the reactor coolant purification system.

第4図は、原子炉冷却材浄化系の熱交換器6,7,CUWポン
プ5を削除し、接続配管20,浄化装置8,戻り配管21のみ
とした変形例である。本実施例では、原子炉通常運転時
には、原子炉冷却材浄化系を運転できない。しかしなが
ら、通常は他にも浄化している系統があり、本浄化系の
予想される浄化寄与率が2%程度であること、また、本
浄化系が対象としているクラツドなどは炉停止時にはく
離して出やすいことを考えると、停止時のみ運転する系
統構造としても、充分に意義はあるものといえる。
FIG. 4 shows a modification in which the heat exchangers 6, 7 and the CUW pump 5 of the reactor coolant purification system are deleted and only the connecting pipe 20, the purifying device 8 and the return pipe 21 are provided. In this embodiment, the reactor coolant purification system cannot be operated during normal reactor operation. However, there are usually other purification systems, and the expected purification contribution rate of this purification system is about 2%. Also, the cladding etc. targeted by this purification system are separated when the reactor is stopped. Considering that it is easy to get out, it can be said that the system structure that operates only when stopped is sufficiently significant.

次に、これまでの実施例で利用してきた残留熱除去系に
代えて、再循環系を利用する発明の一実施例を、第5図
により説明する。
Next, an embodiment of the invention using a recirculation system instead of the residual heat removal system used in the above embodiments will be described with reference to FIG.

本実施例において、浄化すべき炉水は、PLRポンプ2の
下流から取込まれる。図において、15はポンプメンテナ
ンス用止め弁,16は流量調整弁,17はバイパス弁,18は給
水系配管である。
In this embodiment, the reactor water to be purified is taken in from the downstream of the PLR pump 2. In the figure, 15 is a stop valve for pump maintenance, 16 is a flow control valve, 17 is a bypass valve, and 18 is a water supply system piping.

原子炉1内の炉水は、PLRポンプ2により循環させられ
る。この内の一部が流量調整弁16で流量調整後、再生熱
交換器6,非再生熱交換器7において約50℃に冷却され、
浄化装置8で浄化される。浄化水は、原子炉冷却材浄化
系CUWポンプ5により加圧され、再生熱交換器6,給水系
配管18を経て原子炉1に戻される。
The reactor water in the nuclear reactor 1 is circulated by the PLR pump 2. A part of this is cooled to about 50 ° C. in the regenerative heat exchanger 6 and the non-regenerative heat exchanger 7 after the flow rate is adjusted by the flow rate adjusting valve 16,
Purified by the purifying device 8. The purified water is pressurized by the reactor coolant purification system CUW pump 5 and returned to the reactor 1 through the regenerative heat exchanger 6 and the water supply system pipe 18.

本実施例のCUWポンプ5を流れる流体は、浄化装置8に
よりコバルト60等の放射性物質を吸着処理された浄化水
である。従つて、CUWポンプ5は、ポンプ内表面の酸化
被膜中に放射性物質を吸着することがなく、ポンプ5を
定期点検する作業員の被ばく量を低減できる。
The fluid flowing through the CUW pump 5 of the present embodiment is purified water in which radioactive substances such as cobalt 60 have been adsorbed by the purifying device 8. Therefore, the CUW pump 5 does not adsorb radioactive substances in the oxide film on the inner surface of the pump, and can reduce the exposure dose of the worker who regularly inspects the pump 5.

次に、第5図に示した装置の具体的動作例を説明する。Next, a specific operation example of the device shown in FIG. 5 will be described.

(A)原子炉圧力が低い場合 従来例では、原子炉冷却材浄化系は、PLRポンプ2の上
流側に接続していたため、CUWポンプ5の吸込圧力は、
次の様に表わされる。
(A) When the reactor pressure is low In the conventional example, since the reactor coolant purification system was connected to the upstream side of the PLR pump 2, the suction pressure of the CUW pump 5 was
It is expressed as follows.

(ポンプ吸込圧力)=(原子炉ドーム圧力)+(原子炉
水位からCUWポンプ設置位置までの水頭)−(配管圧力
損失)−(熱交換器圧力損失)−(ろ過脱塩装置圧力損
失) ……(1) 現状設計のポンプにおいては、上記吸込圧力が0.6kg/cm
2g以下となつた場合、ポンプ内部にキヤビテーシヨン
が発生し、ポンプケーシング内部およびポンプ羽根の破
損が生じる。プラントの運転モードの中で、NPSHが、こ
の条件を満足できないのは、プラント停止時(原子炉圧
力が大気圧時)の場合であり、約0.5kg/cm2gの圧力不
足となり、浄化運転を継続できない。しかしながら、原
子炉冷却材浄化系は、炉水の浄化を原子炉運転中だけで
なく停止中にも継続しなくてはならないシステムであ
る。
(Pump suction pressure) = (Reactor dome pressure) + (Head from reactor water level to CUW pump installation position)-(Piping pressure loss)-(Heat exchanger pressure loss)-(Filtration desalination unit pressure loss) ... (1) In the currently designed pump, the suction pressure is 0.6 kg / cm
If it is less than 2 g, cavitation occurs inside the pump, and the inside of the pump casing and the pump blades are damaged. In the operation mode of the plant, NPSH cannot satisfy this condition when the plant is stopped (when the reactor pressure is atmospheric pressure), and the pressure is insufficient at about 0.5 kg / cm 2 g, and the purification operation Can't continue. However, the reactor coolant purification system is a system in which purification of reactor water must be continued not only during reactor operation but also during shutdown.

本発明においては、第5図に示す様にPLRポンプ2吐出
圧力を利用してこの問題を解決した。この場合のポンプ
吸込圧力は、(1)式に(PLRポンプ吐出圧力)を加え
たものになる。
In the present invention, this problem is solved by utilizing the discharge pressure of the PLR pump 2 as shown in FIG. In this case, the pump suction pressure is the expression (1) plus (PLR pump discharge pressure).

PLRポンプ2は、プラント運転中だけでなく、プラント
停止中も定格の約20%回転数で常に運転を継続してあ
り、本ポンプ2の吐出圧力は、約0.6kg/cm2g(20%回
転時)である。
The PLR pump 2 is constantly operating not only during plant operation but also during plant stoppage at a rated speed of approximately 20%, and the discharge pressure of this pump 2 is approximately 0.6 kg / cm 2 g (20% When rotating).

従つて、本発明によりプラント停止時(原子炉圧力大気
圧時)においてもCUWポンプ5の運転に必要な吸込圧力
が確保できる。
Therefore, according to the present invention, the suction pressure required for operating the CUW pump 5 can be secured even when the plant is stopped (at the reactor pressure atmospheric pressure).

(B)再循環ポンプが定格回転数で運転中の場合 原子炉圧力が高く原子炉が定格出力で運転中の場合、PL
Rポンプ2は、定格回転数で運転されている。この場
合、PLRポンプ吐出圧力は、約18kg/cm2gであり、原子
炉冷却材浄化系の系統圧力損失(配管機器の圧力損失の
和)値約12kg/cm2gを充分上回るため、浄化系統は、CU
Wポンプ5を停止し、ポンプのバイパス弁17を開いて運
転が可能である。
(B) When the recirculation pump is operating at the rated speed When the reactor pressure is high and the reactor is operating at the rated output, PL
The R pump 2 is operated at the rated speed. In this case, the PLR pump discharge pressure is about 18 kg / cm 2 g, which is sufficiently higher than the system pressure loss (sum of pressure loss of piping equipment) of the reactor coolant purification system of about 12 kg / cm 2 g. System is CU
It is possible to operate by stopping the W pump 5 and opening the pump bypass valve 17.

また、原子炉冷却材浄化系の流量は、原子炉冷却材再循
環系の流量のわずか1〜2%に過ぎず、PLRポンプ2に
よつて浄化流量を確保してもポンプ2のモータ出力に影
響しない。
Further, the flow rate of the reactor coolant purification system is only 1 to 2% of the flow rate of the reactor coolant recirculation system, and even if the purification flow rate is secured by the PLR pump 2, the motor output of the pump 2 is maintained. It does not affect.

従つて、本発明により、プラント運転時にCUWポンプ5
を停止することができる。
Therefore, according to the present invention, the CUW pump 5 is operated during plant operation.
Can be stopped.

(C)CUWポンプメンテナンス時に炉水浄化を行う場合 本実施例においては、原子炉冷却材浄化系の取入れ口を
PLRポンプ2と止め弁15の間に設置することで、CUWポン
プ5のメンテナンス時においても炉水の浄化運転を継続
できる。
(C) When Purifying Reactor Water During CUW Pump Maintenance In this example, the inlet for the reactor coolant purification system was
By installing it between the PLR pump 2 and the stop valve 15, the purifying operation of the reactor water can be continued even during the maintenance of the CUW pump 5.

CUWポンプ5点検時、ポンプ5の出入口弁25を閉じ、バ
イパス弁17を開く。系統の流量は、PLRポンプ2の出口
止め弁15を閉じることでポンプ2により確保できる。
When inspecting the CUW pump 5, the inlet / outlet valve 25 of the pump 5 is closed and the bypass valve 17 is opened. The flow rate of the system can be secured by the pump 2 by closing the outlet stop valve 15 of the PLR pump 2.

PLRポンプ2は、大容量高圧型ポンプであるため、原子
炉冷却材浄化系流量と圧力を確保するためには、ポンプ
回転数を定格の約70%まで上げて圧力を確保し、流量
は、調整弁16で絞り運転しなくてはならない。
Since the PLR pump 2 is a large-capacity high-pressure type pump, in order to secure the reactor coolant purification system flow rate and pressure, increase the pump rotation speed to about 70% of the rating to secure the pressure, and the flow rate is The throttle valve 16 must be throttled.

ここで、PLRポンプ2のメカニカルシール点検に必要な
時間は、CUWポンプ5のメンテナンスに必要な日数と比
べて短時間であるため、本発明により炉水の浄化運転時
間の延長が計れる。
Here, since the time required for the mechanical seal inspection of the PLR pump 2 is shorter than the number of days required for the maintenance of the CUW pump 5, the purifying operation time of the reactor water can be extended by the present invention.

とはいうものの、PLRポンプ2を定格の70%回転数で運
転する場合の必要動力は、CUWポンプ5の定格運転に必
要な動力に比べて非常に大きいため、この運転モードを
ポンプ5のメンテナンス時以外に使用することは、経済
効率上好ましくない、以上述べた運転モードA〜C別に
運転を切換えることが必要である。
However, the required power for operating the PLR pump 2 at 70% of the rated speed is much higher than the power required for the rated operation of the CUW pump 5, so this operating mode is used for pump 5 maintenance. It is necessary to switch the operation for each of the above-mentioned operation modes A to C, which is not preferable in terms of economic efficiency if it is used at other times.

本発明により第7図に示す様に、浄化装置出口側(F
部)の線量は、従来例のA部における線量の約1/100に
低減できる。
According to the present invention, as shown in FIG.
The dose of (part) can be reduced to about 1/100 of the dose in part A of the conventional example.

〔発明の効果〕〔The invention's effect〕

本発明によれば、押込圧力不足の問題点が解消され、CU
Wポンプをろ過脱塩器の下流側に設置できるので、以下
の効果が得られる。
According to the present invention, the problem of insufficient pushing pressure is solved, and the CU
Since the W pump can be installed on the downstream side of the filter demineralizer, the following effects can be obtained.

(1)CUWポンプ内部に蓄積される放射性物質を従来に
比べて約1/100に低減でき、定検時の作業員の被ばく量
を低減可能である。
(1) The radioactive material accumulated inside the CUW pump can be reduced to about 1/100 of that of the conventional method, and the exposure dose to workers during regular inspections can be reduced.

(2)プラント運転中、PLRポンプ吐出圧力を使用して
浄化装置に炉水を供給でき、CUWポンプを停止できるた
めポンプの汚染が生じない。
(2) During the plant operation, reactor water can be supplied to the purifier using the PLR pump discharge pressure, and the CUW pump can be stopped, so the pump does not become contaminated.

(3)CUWポンプメンテナンス時、RHRポンプまたはPLR
ポンプで浄化系の運転を継続できる。
(3) RHR pump or PLR during CUW pump maintenance
The pump can continue to operate the purification system.

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

第1図は本発明により残留熱除去系のポンプを利用した
原子炉冷却材浄化系の一実施例を示す系統図、第2図,
第3図は他の実施例を示す系統図、第4図は第1図実施
例の変形例を示す系統図、第5図は本発明により再循環
系のポンプを利用した原子炉冷却材浄化系の一実施例を
示す系統図、第6図は従来のBWRの一般的系統構成の一
例を示す系統図、第7図はその冷却材浄化系における配
管表面線量率の一例を示すグラフである。 1…原子炉圧力容器、2…再循環(PLR)ポンプ、3…
残留熱除去(RHR)ポンプ、4…残留熱除去系熱交換
器、5…原子炉冷却材浄化系(CUW)ポンプ、6…再生
熱交換器、7…非再生熱交換器、8…浄化装置、9…タ
ービン、10…主復水器、15…ポンプメンテナンス用止め
弁、16…流量調整弁、17…バイパス弁、18…給水系配
管、20…炉水取入れ配管、21…戻り配管、23,24,25…切
換え弁。
FIG. 1 is a system diagram showing an embodiment of a reactor coolant purification system using a residual heat removal system pump according to the present invention, FIG.
FIG. 3 is a system diagram showing another embodiment, FIG. 4 is a system diagram showing a modification of the embodiment shown in FIG. 1, and FIG. 5 is a reactor coolant purification using a recirculation pump according to the present invention. FIG. 6 is a system diagram showing an example of a system, FIG. 6 is a system diagram showing an example of a general system configuration of a conventional BWR, and FIG. 7 is a graph showing an example of pipe surface dose rate in the coolant purification system. . 1 ... Reactor pressure vessel, 2 ... Recirculation (PLR) pump, 3 ...
Residual heat removal (RHR) pump, 4 ... Residual heat removal system heat exchanger, 5 ... Reactor coolant purification system (CUW) pump, 6 ... Regenerative heat exchanger, 7 ... Non-regenerated heat exchanger, 8 ... Purification device , 9 ... Turbine, 10 ... Main condenser, 15 ... Pump maintenance stop valve, 16 ... Flow control valve, 17 ... Bypass valve, 18 ... Water supply system piping, 20 ... Reactor water intake piping, 21 ... Return piping, 23 , 24,25 ... Switching valve.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 白石 忠 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 木下 詳一郎 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 大倉 稔 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 辻 昭夫 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 (56)参考文献 特開 昭54−38498(JP,A) 特開 昭60−17396(JP,A) 特開 昭62−180295(JP,A) 特開 昭62−190496(JP,A) ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Tadashi Shiraishi 1-1-1, Sachimachi, Hitachi City, Ibaraki Hitachi Ltd., Hitachi Works (72) Inventor Shoichiro Kinoshita 3-chome, Hitachi City, Ibaraki Prefecture 1-1 Hitachi Ltd., Hitachi Works, Hitachi Plant (72) Inventor Minoru Okura 3-1-1, Saichocho, Hitachi City, Ibaraki Prefecture Hitachi Ltd., Hitachi Works, Hitachi Plant (72) Inventor Akio Tsuji Hitachi City, Ibaraki Prefecture 3-1, 1-1 Sachimachi, Hitachi, Ltd. Hitachi factory (56) References JP-A-54-38498 (JP, A) JP-A-60-17396 (JP, A) JP-A-62-180295 ( JP, A) JP 62-190496 (JP, A)

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】ポンプと熱交換器と浄化装置とを含み原子
炉通常運転時には再循環系の再循環ポンプの吸込配管側
から炉水を取込み所定温度まで冷却し浄化した後に原子
炉圧力容器に戻す原子炉冷却材浄化系において、前記浄
化系のポンプを前記浄化装置よりも下流に配置するとと
もに、原子炉停止時に前記循環ポンプの吸込配管側に代
えて残留熱除去系ポンプの出口側から炉水を取入れる配
管を設けたことを特徴とする原子炉冷却材浄化系。
1. A reactor pressure vessel, which includes a pump, a heat exchanger, and a purifying device, takes in reactor water from a suction pipe side of a recirculation pump of a recirculation system during normal operation of the reactor, cools it to a predetermined temperature, and purifies it. In the reactor coolant purification system to be returned, the pump of the purification system is arranged downstream of the purification device, and the reactor is installed from the outlet side of the residual heat removal system pump instead of the suction pipe side of the circulation pump when the reactor is stopped. A reactor coolant purification system characterized by the provision of piping for introducing water.
【請求項2】特許請求の範囲第1項において、原子炉停
止時の炉水取入れ配管を前記浄化装置よりも上流の前記
熱交換器入口に接続したことを特徴とする原子炉冷却材
浄化系。
2. A reactor coolant purification system according to claim 1, wherein a reactor water intake pipe when the reactor is shut down is connected to the heat exchanger inlet upstream of the purification device. .
【請求項3】特許請求の範囲第1項において、前記残留
熱除去系が2系統あり、前記炉水取入れ配管を両系統か
ら接続したことを特徴とする原子炉冷却材浄化系。
3. The reactor coolant purification system according to claim 1, wherein the residual heat removal system has two systems and the reactor water intake pipe is connected from both systems.
【請求項4】特許請求の範囲第1項乃至第3項のうちの
いずれか一項において、原子炉停止時に前記浄化系のポ
ンプを系統から切り離す切換え弁を備えたことを特徴と
する原子炉冷却材浄化系。
4. The nuclear reactor according to claim 1, further comprising a switching valve for disconnecting the purification system pump from the system when the reactor is stopped. Coolant purification system.
【請求項5】ポンプと熱交換器と浄化装置とを含み再循
環系から取込んだ炉水を所定温度まで冷却し浄化した後
に原子炉圧力容器に戻す原子炉冷却材浄化系において、
前記浄化系のポンプの前後に切換え弁を配して原子炉通
常運転時にこのポンプをバイパスする弁を並列に設けこ
れらを前記浄化装置よりも下流に配置するとともに、前
記熱交換器への炉水取入れ配管を原子炉停止時に流量を
調節する弁を介して再循環系ポンプの下流に接続したこ
とを特徴とする原子炉冷却材浄化系。
5. A reactor coolant purification system, which includes a pump, a heat exchanger, and a purification device, cools reactor water taken from a recirculation system to a predetermined temperature, purifies it, and then returns it to a reactor pressure vessel,
A switching valve is arranged in front of and behind the purification system pump and valves for bypassing this pump are provided in parallel during normal reactor operation, and these are arranged downstream of the purification device, and the reactor water to the heat exchanger is also provided. A reactor coolant purification system characterized in that an intake pipe is connected downstream of a recirculation system pump through a valve that regulates a flow rate when the reactor is stopped.
JP61060075A 1986-03-18 1986-03-18 Reactor coolant purification system Expired - Lifetime JPH0679073B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61060075A JPH0679073B2 (en) 1986-03-18 1986-03-18 Reactor coolant purification system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61060075A JPH0679073B2 (en) 1986-03-18 1986-03-18 Reactor coolant purification system

Publications (2)

Publication Number Publication Date
JPS62215894A JPS62215894A (en) 1987-09-22
JPH0679073B2 true JPH0679073B2 (en) 1994-10-05

Family

ID=13131600

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61060075A Expired - Lifetime JPH0679073B2 (en) 1986-03-18 1986-03-18 Reactor coolant purification system

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Country Link
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