JPH0454914B2 - - Google Patents
Info
- Publication number
- JPH0454914B2 JPH0454914B2 JP58207154A JP20715483A JPH0454914B2 JP H0454914 B2 JPH0454914 B2 JP H0454914B2 JP 58207154 A JP58207154 A JP 58207154A JP 20715483 A JP20715483 A JP 20715483A JP H0454914 B2 JPH0454914 B2 JP H0454914B2
- Authority
- JP
- Japan
- Prior art keywords
- coolant
- coolant supply
- reactor
- heat exchanger
- regenerative heat
- 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
Links
- 239000002826 coolant Substances 0.000 claims description 74
- 238000000746 purification Methods 0.000 claims description 28
- 230000001172 regenerating effect Effects 0.000 claims description 21
- 238000010612 desalination reaction Methods 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 2
- 230000008646 thermal stress Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000003507 refrigerant Substances 0.000 description 2
- 230000035882 stress Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 230000003252 repetitive effect Effects 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Landscapes
- Structure Of Emergency Protection For Nuclear Reactors (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Description
〔発明の利用分野〕
本発明は、原子炉冷却材供給設備に係り、特に
主循環系冷却材と浄化系冷却材とが合流される合
流配管部を具えた原子炉冷却材供給設備に関す
る。
〔発明の背景〕
原子炉において発生された熱は、熱媒体として
循環される冷却材によつて外部に取り出され、発
電等に用いられる。通常、このとき循環使用され
る冷却材の一部を連続的に抜き出して浄化系にて
浄化した後、これを再び主循環系に合流させるよ
うにしている。このような原子炉冷却材供給設備
の一従来例を沸騰水型原子炉の場合について第1
図の系統構成図により説明する。
第1図において、沸騰水型の原子炉1には、図
示されていない主循環系冷却材供給装置から冷却
材供給主管ライン2を介して主循環系冷却材が供
給される。原子炉1内の冷却材は、再循環ポンプ
3によつて強制的に対流させられるようになつて
いる。この再循環される冷却材の一部所定量が浄
化系循環ポンプ4によつて抜き出され、冷却材浄
化系に導びかれるようになつている。冷却材浄化
系は再生熱交換器5、非再性熱交換機6、過脱
塩装置7等から構成されている。この浄化系に流
入された冷却材は、再生熱交換器5と非再生熱交
換器6とによつて所定温度に冷却された後、過
脱塩器7に流入され、過脱塩器7によつて浄化
された冷却材は、前記浄化系循環ポンプ4によつ
て昇圧され、前記再生熱交換器5によつて加熱さ
れた後、冷却材供給主管ライン2に設けられてい
る合流管部8に流入される。
このように構成された従来の原子炉冷却材供給
設備にあつては、通常運転時における冷却材浄化
系からの戻り冷却材の温度と主循環系冷却材の温
度とは、ほぼ同等になるように制御され合流され
るようになつている。
しかし、原子炉起動、停止または高温待機(原
子炉出力を出さずに運転継続する態様)の期間に
おいては、合流されるこれらの冷却材の温度バラ
ンスがくずれ、主循環系冷却材供給主管ラインの
温度が40℃以下となるのに対して浄化系からの冷
却材の温度は220℃以上となることがある。
このように温度差が180℃以上にも達する二つ
の流体が合流されると、合流配管部8においては
局所的に非常に大きな温度差を持つ部分が発生し
これによつて非常に大きな熱応力が作用すること
になる。合流配管部8の管壁(冷却材に接触して
いる側)の任意の一点に作用する熱応力は、合流
流体の流れ挙動に応じて大きく変化する繰返し応
力となる。しかも、この応力は原子炉の起動及び
停止等の度に繰返し作用するので、合流配管部8
に高サイクル熱疲労によるクラツク等の損傷が発
生する恐れがある。
そこで従来、合流配管部8をサーマルスリーブ
構造のものとすることによつて、主要部の熱応力
を緩和して熱疲労を低減させ、クラツク等の損傷
を防止しようとすることが行なわれている。しか
し、起動または停止時の期間に生ずる如き非常に
大きな温度差による高サイクル熱疲労を、サーマ
ルスリーブ構造だけで吸収させることは困難であ
り、上記損傷を十分に防止させることができない
という欠点があつた。
第2図はこの欠点を補なうために考えられた原
子炉冷却材供給設備の従来例を示す。第2図に示
す原子炉冷却材供給設備は、前述第1図の原子炉
冷却材供給設備において高サイクル熱疲労による
クラツク等の損傷が発生する恐れの強い運転モー
ドすなわち原子炉起動、停止または高温待機時に
は、浄化後の冷却材を再生熱交換器5により加熱
せずに、切換弁9,10によりバイパスライン1
1に通水させ、主循環系冷却材供給主管ライン2
に設けられている合流配管部8に流入させる系統
構成としており、これにより合流配管部8におい
て合流される夫々の冷却材の温度のバランスを保
ち、過大な熱応力の発生を防止するものである。
しかし、第2図に示す原子炉冷却材供給設備
は、再生熱交換器5により浄化系戻り冷却材の加
熱を行なわないため、第1図に示す原子炉冷却材
供給設備と比較して、合流配管部8から原子炉1
に至る間の冷却材温度が低下し熱効率が低下する
と同時に、原子炉ノズル12において炉水との温
度差による高サイクル熱疲労の恐れが大きくな
り、また、浄化系循環ポンプ4によつて抜き出さ
れ冷却材浄化装置に導びかれる冷却材が再生熱交
換器5にて冷却されないので、これを所定温度に
冷却後過脱塩装置7に流入させるためには、非
再生熱交換器6の容量増大が必要になるという問
題があつた。
〔発明の目的〕
本発明の目的は、如上の問題を伴うことなく、
浄化系冷却材を主循環系冷却材に合流させる合流
配管部の熱疲労を大幅に低減でき、合流配管部の
高サイクル熱疲労による損傷を防止できる原子炉
冷却材供給設備を提供することにある。
〔発明の概要〕
本発明は、主循環系冷却材供給主管ラインと、
再生熱交換器、非再生熱交換器および過脱塩器
を有する浄化系と、この浄化系の過脱塩器通過
後に該再生熱交換器内の戻り側を経た浄化系戻り
冷却材を主循環系冷却材供給主管ラインに合流さ
せる合流部とからなる原子炉冷却材供給設備にお
いて、主循環系冷却材供給主管ラインから分岐し
て上記再生熱交換器内の戻り側と過脱塩器の上
流側との間の浄化系流路へバイパスするバイパス
ラインと、該バイパスライン中に設けられた常時
は閉である弁と、主循環系冷却材供給主管ライン
中に該バイパスライン分岐点より下流側に設けら
れた常時は開である弁と、主循環系冷却材供給主
管ライン中の冷却材の流量および温度が夫々所定
値より低下したときに上記前者の弁を開に、後者
の弁を閉にする自動制御装置とを備えたことを特
徴とするものである。
〔発明の実施例〕
本発明の一実施例を第3図により説明する。図
中、第1図の従来例と同一構成・同一機能の部分
は同一符号で示し、その説明は省略する。
第3図においては、第1図に示した従来例と異
なり、浄化系の戻り冷却材が再生熱交換器5を通
過する手前の合流配管部22にて浄化系戻りライ
ン13へバイパスするライン14が冷却材供給主
管ライン2から分岐しており、このバイパスライ
ン14及びその分岐部より下流側の冷却材供給主
管ライン2に夫々自動弁15及び16が設けら
れ、またバイパスライン14上に逆止弁23が設
けられている。また、冷却材供給主管ライン2に
主循環系の冷却材供給量および温度を夫々検出す
る流量検出器17と温度検出器18とが設けら
れ、それらの検出器17,18から出力される流
量信号Fおよび温度信号Tは、それぞれ比較器1
9,20に入力されている。比較器19,20の
他の入力端には、予め設定された基準流量信号
F0と基準温度信号T0とが入力されている。比較
器19,20はそれぞれ入力信号FがF0以下に
なつた時、且つ入力信号TがT0以下になつた時、
自動弁15を開、16を閉とする論理信号を出力
するように構成されている。この比較器19,2
0の出力信号はAND回路21を介して自動弁1
5,16に入力されている。
このように構成された本発明実施例の動作を以
下に説明する。
通常運転時にあつては、主循環系の冷却材供給
主管ライン2から供給される冷却材は約210℃に
昇温されている。一方、浄化系からの戻り冷却材
も約225℃に昇温されている。それらの冷却材は
合流配管部8で合流され、原子炉1内に供給され
る。すなわち、このとき自動弁15は閉、16は
開となつている。
ところが、原子炉1の起動時、停止時または高
温待機時にあつては、第1表に例示されているよ
うに、主循環系から供給される冷却材の流量は、
定格運転時の2%程度に低減され、しかもその温
度は38℃程度に低下される。一方、浄化系戻り冷
却材の温度は上記の約225℃に維持されたままで
ある。このように温度差大なる二つの冷却材が合
流配管部8に流入すると、前述したように高サイ
クル熱疲労による損傷発生につながる危険性が大
となる。
[Field of Application of the Invention] The present invention relates to a nuclear reactor coolant supply facility, and more particularly to a nuclear reactor coolant supply facility including a merging piping section where a main circulation system coolant and a purification system coolant are merged. [Background of the Invention] Heat generated in a nuclear reactor is extracted to the outside by a coolant that is circulated as a heat medium and used for power generation or the like. Normally, a part of the coolant that is circulated at this time is continuously extracted and purified in a purification system, and then is allowed to join the main circulation system again. A conventional example of such reactor coolant supply equipment is described in Part 1 for a boiling water reactor.
This will be explained using the system configuration diagram shown in the figure. In FIG. 1, a main circulation system coolant is supplied to a boiling water type nuclear reactor 1 from a main circulation system coolant supply device (not shown) via a main coolant supply pipe line 2. In FIG. The coolant in the reactor 1 is forced to convect by a recirculation pump 3. A predetermined amount of this recirculated coolant is extracted by a purification system circulation pump 4 and guided to the coolant purification system. The coolant purification system is composed of a regenerative heat exchanger 5, a non-regenerative heat exchanger 6, a super desalination device 7, and the like. The coolant flowing into the purification system is cooled to a predetermined temperature by the regenerative heat exchanger 5 and the non-regenerative heat exchanger 6, and then flows into the super-demineralizer 7. The thus purified coolant is pressurized by the purification system circulation pump 4, heated by the regenerative heat exchanger 5, and then transferred to the confluence pipe section 8 provided in the main coolant supply pipe line 2. is flowing into the country. In conventional reactor coolant supply equipment configured in this way, the temperature of the return coolant from the coolant purification system and the temperature of the main circulation system coolant during normal operation are almost the same. It is now controlled and merged. However, during reactor start-up, shutdown, or high-temperature standby (continuation of operation without reactor output), the temperature balance of these combined coolants is disrupted, and the main circulation system coolant supply pipe line is affected. While the temperature may be below 40°C, the temperature of the coolant from the purification system may be above 220°C. When two fluids with a temperature difference of 180°C or more are merged in this way, a region with a very large temperature difference locally occurs in the merging piping section 8, resulting in a very large thermal stress. will come into play. The thermal stress acting on any one point on the pipe wall (the side in contact with the coolant) of the confluence piping section 8 becomes a repetitive stress that changes significantly depending on the flow behavior of the confluence fluid. Moreover, since this stress acts repeatedly every time the reactor is started and stopped, the merging piping section 8
Damage such as cracks may occur due to high cycle thermal fatigue. Conventionally, attempts have been made to provide the confluence piping section 8 with a thermal sleeve structure to alleviate thermal stress in the main section, reduce thermal fatigue, and prevent damage such as cracks. . However, it is difficult to absorb high-cycle thermal fatigue due to extremely large temperature differences such as those that occur during startup or shutdown using only the thermal sleeve structure, and there is a drawback that the above-mentioned damage cannot be sufficiently prevented. Ta. FIG. 2 shows a conventional example of reactor coolant supply equipment designed to compensate for this drawback. The reactor coolant supply equipment shown in Figure 2 is designed to operate in the same operating mode as the reactor coolant supply equipment shown in Figure 1, which is likely to cause damage such as cracks due to high-cycle thermal fatigue, i.e., reactor startup, shutdown, or high-temperature operation. During standby, the purified coolant is not heated by the regenerative heat exchanger 5, and the bypass line 1 is
1 and the main circulation system coolant supply main pipe line 2.
The system has a system configuration in which the coolant flows into the confluence piping section 8 provided in the confluence piping section 8, thereby maintaining the temperature balance of the respective coolants that are merged in the confluence piping section 8 and preventing the generation of excessive thermal stress. . However, since the reactor coolant supply equipment shown in FIG. 2 does not heat the purification system return coolant using the regenerative heat exchanger 5, the reactor coolant supply equipment shown in FIG. From piping section 8 to reactor 1
At the same time, the risk of high-cycle thermal fatigue due to the temperature difference between the reactor nozzle 12 and the reactor water increases. Since the refrigerant is not cooled by the regenerative heat exchanger 5 and is led to the refrigerant purification device, it is necessary to increase the capacity of the non-regenerative heat exchanger 6 in order to cool it to a predetermined temperature and then flow it into the over-desalination device 7. The problem was that it needed to be increased. [Object of the Invention] The object of the present invention is to solve the problem without the above-mentioned problems.
An object of the present invention is to provide reactor coolant supply equipment that can significantly reduce thermal fatigue of a merging piping section that joins purification system coolant with main circulation system coolant, and can prevent damage to the merging piping section due to high-cycle thermal fatigue. . [Summary of the Invention] The present invention provides a main circulation system coolant supply main pipe line;
A purification system having a regenerative heat exchanger, a non-regenerative heat exchanger, and a super-demineralizer, and a main circulation of the purification system return coolant that passes through the super-demineralizer of this purification system and passes through the return side in the regenerative heat exchanger. In the reactor coolant supply equipment, which consists of a merging section that joins the system coolant supply main pipe line, it branches from the main circulation system coolant supply main pipe line to the return side in the regenerative heat exchanger and upstream of the super desalination device. A bypass line that bypasses the purification system flow path between the side and the normally closed valve provided in the bypass line, and a valve located downstream of the bypass line branch point in the main circulation system coolant supply main pipe line. When the flow rate and temperature of the coolant in the main circulation system coolant supply pipe line drop below predetermined values, the former valve is opened and the latter valve is closed. The invention is characterized in that it is equipped with an automatic control device that performs the following functions. [Embodiment of the Invention] An embodiment of the present invention will be described with reference to FIG. In the figure, parts having the same configuration and function as those of the conventional example shown in FIG. In FIG. 3, unlike the conventional example shown in FIG. 1, a line 14 bypasses the return coolant from the purification system to the purification system return line 13 at the confluence piping section 22 before passing through the regenerative heat exchanger 5. is branched from the main coolant supply line 2, and automatic valves 15 and 16 are provided on this bypass line 14 and the main coolant supply line 2 downstream from the branch, respectively. A valve 23 is provided. Further, the main coolant supply pipe line 2 is provided with a flow rate detector 17 and a temperature detector 18 for detecting the coolant supply amount and temperature of the main circulation system, respectively, and the flow rate signals output from these detectors 17 and 18 are provided. F and temperature signal T are each output from comparator 1
9 and 20. The other input terminals of the comparators 19 and 20 are connected to a preset reference flow rate signal.
F 0 and reference temperature signal T 0 are input. Comparators 19 and 20 operate when the input signal F becomes less than F 0 and when the input signal T becomes less than T 0 , respectively.
It is configured to output a logic signal that opens the automatic valve 15 and closes the automatic valve 16. This comparator 19,2
The output signal of 0 is sent to automatic valve 1 via AND circuit 21.
5 and 16. The operation of the embodiment of the present invention configured in this manner will be described below. During normal operation, the coolant supplied from the coolant supply main pipe line 2 of the main circulation system is heated to about 210°C. Meanwhile, the temperature of the return coolant from the purification system is also raised to approximately 225°C. These coolants are combined in a confluence piping section 8 and supplied into the reactor 1. That is, at this time, automatic valve 15 is closed and automatic valve 16 is open. However, when the reactor 1 is started, stopped, or is in high-temperature standby, the flow rate of the coolant supplied from the main circulation system is as shown in Table 1.
The temperature is reduced to about 2% of the rated operating temperature, and furthermore, the temperature is reduced to about 38°C. Meanwhile, the temperature of the purification system return coolant remains maintained at the above-mentioned approximately 225°C. When two coolants with such a large temperature difference flow into the confluence piping section 8, there is a great risk of damage occurring due to high-cycle thermal fatigue, as described above.
本発明によれば、熱効率の低下、原子炉ノズル
における高サイクル熱疲労の危険性増加及び浄化
系の非再生熱交換器の容量増大を伴なわずに、浄
化系戻り冷却材を主循環系冷却材に合流させる合
流配管部の熱疲労を大幅に低減することができ、
合流配管部の高サイクル熱疲労による損傷を防止
でき、これによつて、原子炉プラントの信頼性及
び稼動率が向上する。
According to the present invention, purification system return coolant can be used to cool the main circulation system without reducing thermal efficiency, increasing the risk of high cycle thermal fatigue in the reactor nozzle, and increasing the capacity of the purification system non-regenerative heat exchanger. Thermal fatigue of the confluence piping section that joins the material can be significantly reduced,
Damage to the merging piping due to high-cycle thermal fatigue can be prevented, thereby improving the reliability and availability of the nuclear reactor plant.
第1図及び第2図は、従来の原子炉冷却材供給
設備の系統構成図、第3図及び第4図は夫々本発
明の異なる実施例を示す系統構成図である。
1…原子炉、2…冷却材供給主管ライン、5…
再生熱交換器、6…非再生熱交換器、7…過脱
塩装置、8…合流配管部、12…原子炉ノズル、
13…浄化系戻りライン、14…バイパスライ
ン、15,16…自動弁、17…流量検出器、1
8…温度検出器、19,20…比較器、21…
AND回路、22…バイパスライン流入部、23
…逆止弁、24…浄化系行きライン。
1 and 2 are system configuration diagrams of conventional nuclear reactor coolant supply equipment, and FIGS. 3 and 4 are system configuration diagrams showing different embodiments of the present invention, respectively. 1... Nuclear reactor, 2... Coolant supply main line, 5...
Regenerative heat exchanger, 6... Non-regenerative heat exchanger, 7... Super desalination device, 8... Merging piping section, 12... Reactor nozzle,
13...Purification system return line, 14...Bypass line, 15, 16...Automatic valve, 17...Flow rate detector, 1
8... Temperature detector, 19, 20... Comparator, 21...
AND circuit, 22... Bypass line inflow section, 23
...Check valve, 24...Line to the purification system.
Claims (1)
供給主管ラインと;原子炉内から抜き出された一
部の冷却材が順に流れる再生熱交換器、非再生熱
交換器および過脱塩器を含み、過脱塩器通過
後の冷却材が該再生熱交換器内の戻り側を経て流
れるようにした浄化系と化系の該再生熱交換器内
の戻り側を通過した冷却材を主循環系冷却材主管
ラインに合流させる合流部と;からなる原子炉冷
却材供給設備において、主循環系冷却材供給主管
ラインから分岐して上記再生熱交換器内の戻り側
と過脱塩器の上流側との間の浄化系流路へバイ
パスするバイパスラインと、該バイパスライン中
に設けられた常時は閉である弁と、主循環系冷却
材供給主管ラインの該バイパスライン分岐点より
下流側にて主循環系冷却材供給主管ライン中に設
けられ常時は開である弁と、主循環系冷却材供給
主管ライン中の冷却材の流量および温度が夫々所
定値より低下したときに上記前者の弁を開に、後
者の弁を閉にする自動制御装置と、を備えたこと
を特徴とする原子炉冷却材供給設備。1 Main circulation system coolant supply main line that supplies coolant into the reactor; regenerative heat exchanger, non-regenerative heat exchanger, and over-desalination through which some of the coolant extracted from the reactor flows in order. A purification system including a demineralizer, in which the coolant that has passed through the over-desalination device flows through the return side of the regenerative heat exchanger, and a purification system that allows the coolant that has passed through the return side of the regenerative heat exchanger of the purification system to flow through the return side of the regenerative heat exchanger. In the reactor coolant supply equipment, the reactor coolant supply equipment consists of: a confluence section that joins the main circulation system coolant main pipe line; A bypass line that bypasses the purification system flow path between the upstream side of On the side, there is a valve that is installed in the main circulation system coolant supply main line and is normally open, and a valve that is installed in the main circulation system coolant supply main line when the flow rate and temperature of the coolant in the main circulation system coolant supply main line fall below predetermined values. A nuclear reactor coolant supply facility characterized by comprising: an automatic control device that opens one valve and closes the other valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58207154A JPS60100095A (en) | 1983-11-04 | 1983-11-04 | Reactor coolant supply equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58207154A JPS60100095A (en) | 1983-11-04 | 1983-11-04 | Reactor coolant supply equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60100095A JPS60100095A (en) | 1985-06-03 |
| JPH0454914B2 true JPH0454914B2 (en) | 1992-09-01 |
Family
ID=16535113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58207154A Granted JPS60100095A (en) | 1983-11-04 | 1983-11-04 | Reactor coolant supply equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60100095A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06105314B2 (en) * | 1985-10-17 | 1994-12-21 | 株式会社日立製作所 | Reactor coolant purification system |
-
1983
- 1983-11-04 JP JP58207154A patent/JPS60100095A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60100095A (en) | 1985-06-03 |
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