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JPH0151792B2 - - Google Patents
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JPH0151792B2 - - Google Patents

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Publication number
JPH0151792B2
JPH0151792B2 JP56079346A JP7934681A JPH0151792B2 JP H0151792 B2 JPH0151792 B2 JP H0151792B2 JP 56079346 A JP56079346 A JP 56079346A JP 7934681 A JP7934681 A JP 7934681A JP H0151792 B2 JPH0151792 B2 JP H0151792B2
Authority
JP
Japan
Prior art keywords
sodium
temperature
heat exchanger
intermediate heat
primary
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
Application number
JP56079346A
Other languages
Japanese (ja)
Other versions
JPS57194387A (en
Inventor
Seigo Yamakawa
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
Original Assignee
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 Ltd filed Critical Hitachi Ltd
Priority to JP56079346A priority Critical patent/JPS57194387A/en
Publication of JPS57194387A publication Critical patent/JPS57194387A/en
Publication of JPH0151792B2 publication Critical patent/JPH0151792B2/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

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

【発明の詳細な説明】 本発明はタンク型高速炉に使用するに好適な原
子炉主容器に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a reactor main vessel suitable for use in a tank-type fast reactor.

ナトリウム冷却タンク型高速炉に於ては、原子
炉主容器内に、炉心、複数個の中間熱交換器及び
複数個の1次側主循環ポンプが設置されている。
更に、原子炉主容器内には、炉心より流出する高
温の1次ナトリウムと中間熱交換器より流出する
低温の1次ナトリウムとを分離し炉心冷却パスを
形成する熱遮蔽構造物が設置されている。従来よ
り、この原子炉主容器の製作に於ては、解決すべ
きいくつかの問題点があつた。その一つは、炉心
より流出する1次側ナトリウム温度の過渡変化に
関するものである。即ち、原子炉をスクラムする
ような過渡運転時には、炉心より流出する1次ナ
トリウムの流路を構成するホツトプレナムにおい
て、一次ナトリウムが高温から低温に変化するこ
とに伴つて生じる1次ナトリウムの密度変化の影
響によつて、前記ホツトプレナムの上部に密度の
小さい高温のナトリウムが停留するいわゆるスト
ラテイフイケーシヨン(温度分布の成層現象)が
生じ、中間熱交換器へ流入する1次ナトリウムの
温度変化が過酷となり、中間熱交換器内部の熱衝
撃を増大させるという欠点がある。
In a sodium cooled tank type fast reactor, a reactor core, a plurality of intermediate heat exchangers, and a plurality of primary side main circulation pumps are installed in the reactor main vessel.
Furthermore, a thermal shielding structure is installed inside the reactor main vessel to separate the high temperature primary sodium flowing out from the reactor core from the low temperature primary sodium flowing out from the intermediate heat exchanger, forming a core cooling path. There is. Conventionally, there have been several problems that must be solved in the manufacture of this nuclear reactor main vessel. One of these concerns transient changes in the temperature of the primary sodium flowing out from the core. In other words, during transient operations such as scramming a nuclear reactor, changes in density of primary sodium occur as the temperature changes from high temperature to low temperature in the hot plenum, which constitutes the flow path for primary sodium flowing out from the core. As a result, a so-called stratification phenomenon occurs in which low-density, high-temperature sodium remains in the upper part of the hot plenum, resulting in severe temperature changes in the primary sodium flowing into the intermediate heat exchanger. , which has the disadvantage of increasing the thermal shock inside the intermediate heat exchanger.

本発明の目的は、前記ホツトプレナム内の1次
ナトリウムの温度変化に伴つて生じるストラテイ
フイケーシヨンを効果的に抑制することにより前
記欠点を生じない良好なタンク型原子炉を提供す
ることにある。
An object of the present invention is to provide a good tank-type nuclear reactor that does not suffer from the above-mentioned drawbacks by effectively suppressing the strategy-ication that occurs as a result of temperature changes in the primary sodium within the hot plenum.

本発明は、前記ホツトプレナム内を流れる1次
ナトリウムのストラテイフイケーシヨンを数値実
験により確認し、更に、ストラテイフイケーシヨ
ンが、中間熱交換器へ流入する1次ナトリウムの
過渡温度変化を大きくし、中間熱交換器内部構造
物への熱衝撃を過大にすることを理論により確認
し、このストラテイフイケーシヨンを抑制する手
段として、中間熱交換器を円筒でカバーし、この
円筒と中間熱交換器とで構成されるアニユラス状
の流路にホツトプレナム上部に高温ナトリウムと
ホツトプレナム下部の低温ナトリウムを流入させ
て上部と下部のナトリウムを混合させることによ
り、中間熱交換器に流入する1次ナトリウムの温
度変化を緩和することを特徴とするものである。
The present invention confirms the strategy of the primary sodium flowing in the hot plenum through numerical experiments, and furthermore, the strategy increases the transient temperature change of the primary sodium flowing into the intermediate heat exchanger, It was confirmed theoretically that the thermal shock to the internal structure of the intermediate heat exchanger would be excessive, and as a means to suppress this strategy, the intermediate heat exchanger was covered with a cylinder, and the cylinder and the intermediate heat exchanger were By flowing high-temperature sodium into the upper part of the hot plenum and low-temperature sodium at the lower part of the hot plenum into an annulus-shaped flow path consisting of a It is characterized by alleviating the

第1図、第2図は、本発明が適用される公知の
タンク型原子炉主容器を示したものである。主容
器1には、炉内と外界とを隔離すると共に構造物
を搭載するルーフスラブ2、複数個の中間熱交換
器7、複数個の1次主循環ポンプ8、炉心5が収
納されている。炉心5は炉心支持構造物3で支持
されている。また、炉の出力を制御する制御棒な
どで構成されている炉心上部機構6が設置されて
いる。炉心5より流出する高温ナトリウムを収容
するホツトプレナム9と中間熱交換器より流出す
る低温ナトリウムを収容するコールドプレナム1
0とは熱遮蔽構造物4で分離されている。炉心よ
り流出した1次ナトリウムは中間熱交換器7と1
次ナトリウム誘導用円筒18で構成されるアニユ
ラム部を一旦上昇した後、1次ナトリウム流入窓
13より伝熱管群19に流入し伝熱管内を流れる
2次ナトリウムに熱を与えながら流下し1次ナト
リウム流出窓14よりコルトプレナム10に流出
する。この1次ナトリウムは1次主循環ポンプ8
より炉心5へ送られる。一方、2次ナトリウムは
下降管15を流下した後、2次側下部プレナム1
6で複数本の伝熱管へ分配される。各伝熱管内に
分配された2次ナトリウムは1次ナトリウムより
熱を受けながら上昇し、2次側上部プレナム17
で合流し、2次側出口ノズル23から蒸気発生器
系へ送られる。第3図は原子炉出力が急減に低下
し1次ナトリウムが高温から低温に変化した時の
ホツトプレナム9における1次ナトリウムの流れ
の様子を示したものである。即ち、原子炉出力が
急速に低下すると炉心出口における1次ナトリウ
ムの温度も高温から低温に変化する。この時のホ
ツトプレナム9でのナトリウムの流動状況は、同
図の矢印で示したように密度の小さい高温ナトリ
ウムが自由液面11に近い上部に滞留し2次流れ
21が生じる。一方、炉心より流出した低温のナ
トリウムはホツトプレナム内で十分に混合しない
まま1次ナトリウムの主流20に沿つて中間熱交
換器7に流入する。このため、中間熱交換器7に
は、1次ナトリウムによる過酷なコールドシヨツ
クが加わり、中間熱交換器内部構造物に不必要な
熱応力が発生する。更に、自由液面11から下方
に沿つて不均一のナトリウム温度分布が生じ、中
間熱交換器7、炉上部機構6、1次主循環ポンプ
8にも温度分布が生じ不必要な熱応力が発生す
る。本発明は上記欠点の原因となるストラテイフ
イケーシヨンを防止するのに好適なタンク型原子
炉主容器を提供するにある。第4図は本発明の実
施例を示したものである。即ち、原子炉の主容器
内を自由液面11を有するホツトプレナム9とコ
ールドプレナム10とに区画する熱遮蔽構造物4
と、前記主容器の上部を閉鎖するルーフスラブ2
と、前記ルーフスラブ2を貫通して一次ナトリウ
ム流入窓13が前記自由液面11下の前記ホツト
プレナム9に一次ナトリウム流出窓14が前記コ
ールドプレナム10内に開口している中間熱交換
器7と、前記中間熱交換器7の一次ナトリウム流
入窓13の外周囲を隙間Aを保つて取り囲む一次
ナトリウム誘導用円筒18とからなる原子炉にお
いて、前記一次ナトリウム誘導用円筒18の下端
よりも下方から上方にわたり前記一次ナトリウム
誘導用円筒18の外周囲を前記熱遮蔽構造物4に
固定手持したストラテイフイケーシヨン防止用円
筒22で隙間Bを保つて囲み、前記ストラテイフ
イケーシヨン防止用円筒22の前記熱遮蔽構造物
4寄り部位とその部位よりも上方の部位とに前記
ホツトプレナム9内の流体の流入口26,27を
備える。このストラテイフイケーシヨン防止用円
筒22は、円周方向にほぼ等間隔に配置した脚柱
24に溶接で固定され、その脚柱24が熱遮蔽構
造物4へ溶接により固定されることにより固定支
持される。そして、流路と成る隙間Bが維持され
るように円周方向にほぼ等間隔に水平突起状のス
ペーサ25がストラテイフイケーシヨン防止用円
筒22に溶接で固定されている。
1 and 2 show a known tank-type nuclear reactor main vessel to which the present invention is applied. The main vessel 1 houses a roof slab 2 that isolates the inside of the reactor from the outside world and mounts structures, a plurality of intermediate heat exchangers 7, a plurality of primary main circulation pumps 8, and a reactor core 5. . The core 5 is supported by a core support structure 3. Additionally, a core upper mechanism 6 is installed, which is comprised of control rods and the like that control the output of the reactor. A hot plenum 9 that accommodates high-temperature sodium flowing out from the reactor core 5 and a cold plenum 1 that accommodates low-temperature sodium flowing out from the intermediate heat exchanger.
0 by a heat shield structure 4. The primary sodium flowing out from the core is transferred to intermediate heat exchangers 7 and 1.
After once ascending through the annular unit composed of the secondary sodium induction cylinder 18, the primary sodium flows into the heat transfer tube group 19 through the primary sodium inflow window 13, and flows down while giving heat to the secondary sodium flowing inside the heat transfer tubes. It flows out into the Kort plenum 10 through the outflow window 14. This primary sodium is supplied to the primary main circulation pump 8.
It is sent to the reactor core 5. On the other hand, after the secondary sodium flows down the downcomer pipe 15, it flows into the secondary lower plenum 1.
6, the heat is distributed to a plurality of heat transfer tubes. The secondary sodium distributed in each heat exchanger tube rises while receiving heat from the primary sodium, and rises to the secondary side upper plenum 17.
and is sent to the steam generator system from the secondary outlet nozzle 23. FIG. 3 shows the flow of primary sodium in the hot plenum 9 when the reactor power suddenly decreases and the primary sodium changes from high temperature to low temperature. That is, when the reactor power rapidly decreases, the temperature of the primary sodium at the reactor core outlet also changes from high temperature to low temperature. At this time, the sodium flow condition in the hot plenum 9 is such that high-temperature sodium with low density stays in the upper part near the free liquid level 11, and a secondary flow 21 is generated, as shown by the arrow in the figure. On the other hand, low-temperature sodium flowing out of the core flows into the intermediate heat exchanger 7 along the primary sodium main stream 20 without being sufficiently mixed within the hot plenum. Therefore, a severe cold shock due to the primary sodium is applied to the intermediate heat exchanger 7, and unnecessary thermal stress is generated in the internal structure of the intermediate heat exchanger. Furthermore, an uneven sodium temperature distribution occurs downward from the free liquid level 11, and temperature distribution also occurs in the intermediate heat exchanger 7, the upper furnace mechanism 6, and the primary main circulation pump 8, causing unnecessary thermal stress. do. The object of the present invention is to provide a tank-type nuclear reactor main vessel that is suitable for preventing the stratification that causes the above-mentioned drawbacks. FIG. 4 shows an embodiment of the present invention. That is, the heat shielding structure 4 divides the inside of the main reactor vessel into a hot plenum 9 and a cold plenum 10 having a free liquid level 11.
and a roof slab 2 for closing the upper part of the main container.
and an intermediate heat exchanger 7 which penetrates the roof slab 2 and has a primary sodium inflow window 13 opening into the hot plenum 9 below the free liquid level 11 and a primary sodium outflow window 14 opening into the cold plenum 10; In a nuclear reactor comprising a primary sodium induction cylinder 18 surrounding the outer periphery of the primary sodium inflow window 13 of the intermediate heat exchanger 7 with a gap A maintained, the primary sodium induction cylinder 18 extends from below to above the lower end of the primary sodium induction cylinder 18. The outer periphery of the primary sodium induction cylinder 18 is surrounded by a strategy cation prevention cylinder 22 fixedly held on the heat shielding structure 4 while maintaining a gap B, and the strategy cation prevention cylinder 22 is shielded from heat. Fluid inlets 26 and 27 in the hot plenum 9 are provided at a portion near the structure 4 and at a portion above that portion. This strafication prevention cylinder 22 is fixed by welding to pedestals 24 arranged at approximately equal intervals in the circumferential direction, and the pedestals 24 are fixed to the heat shielding structure 4 by welding to provide fixed support. be done. Horizontal protruding spacers 25 are welded to the stratification prevention cylinder 22 at approximately equal intervals in the circumferential direction so that the gap B forming the flow path is maintained.

このような構成においては、自由液面11近く
で停留している高温ナトリウムは上部の流入口2
6から隙間B内に入り、比較的低温のナトリウム
は流入口27から入り、これら高低温両ナトリウ
ムは一次ナトリウム誘導用円筒18の下端で合流
混合して均温化され、均温化されたナトリウムは
隙A内を上昇してその上昇過程でより良く均温化
されついには一次ナトリウム流入窓13に流入し
ていく。
In such a configuration, the high temperature sodium that remains near the free liquid level 11 flows through the upper inlet 2.
6 into the gap B, relatively low-temperature sodium enters from the inlet 27, and both high and low-temperature sodium are merged and mixed at the lower end of the primary sodium induction cylinder 18, and the temperature is homogenized. Sodium rises in the gap A, becomes more uniform in temperature during the rising process, and finally flows into the primary sodium inflow window 13.

本発明の効果を第6図に示すモデルで説明す
る。第3図のホツトプレナム9でのナトリウムの
主流20、混合流れ23の存在する領域及び2次
流れ21の存在する領域はそれぞれ第6図の主流
Qa、混合領域Va、死水領域Vbに対応する。さら
に第6図においては炉心出口での流れがホツトプ
レナム内で混合しないまま中間熱交換器に流入す
るバイパス流れQbも考慮してある。このホツト
プレナム内での流れを単純化した物理モデルによ
ると混合域でのエネルギ収支は次式で与えられ
る。
The effects of the present invention will be explained using a model shown in FIG. The main stream 20 of sodium, the area where the mixed flow 23 exists, and the area where the secondary flow 21 exists in the hot plenum 9 in FIG. 3 are the main stream in FIG. 6, respectively.
It corresponds to Q a , mixed region V a , and dead water region V b . Furthermore, in FIG. 6, a bypass flow Q b is also considered in which the flow at the core exit flows into the intermediate heat exchanger without being mixed in the hot plenum. According to a simplified physical model of the flow within this hot plenum, the energy balance in the mixing zone is given by the following equation.

ρCdθa/dt=ρQa(θp−θa)……(1) ただし 初期条件;θa(O)=0 ……(2) 入口温度;θp ……(3) 式(1)の解は次式で与えられる。 ρCdθ a /dt=ρQ ap −θ a )...(1) However, initial condition; θ a (O)=0...(2) Inlet temperature; θ p ...(3) Equation (1) The solution is given by the following equation.

θa/θb=1−e-Qat/Qb ……(4) 一方、全流量の収支は次式で表わされる。 θ ab = 1−e -Qat/Qb (4) On the other hand, the balance of total flow rate is expressed by the following equation.

Q=Qa+Qb ……(5) また、全容積Vと死水領域Vb、混合領域Va
の関係は次式で与えられる。
Q=Q a +Q b (5) Moreover, the relationship between the total volume V, the dead water area V b , and the mixing area V a is given by the following equation.

V=Va+Vb ……(6) 中間熱交換器入口の温度(θ)は次のエネルギ
収支式から求められる。
V=V a +V b (6) The temperature (θ) at the inlet of the intermediate heat exchanger can be obtained from the following energy balance equation.

Qθ=Qaθa+Qbθp ……(7) したがつて、無次元化した中間熱交換器出口温
度θ*は次式で求められる。
Qθ=Q a θ a +Q b θ p (7) Therefore, the dimensionless intermediate heat exchanger outlet temperature θ * can be obtained by the following equation.

θ*=1−Qa/Qe-Qa/QV/Vat*……(8) ただし θ*=(θp−θ)/(θp−θa(O)) ……(9) t*=V/Q 第7図は式(8)においてQa/Qb=1としたとき
の中間熱交換器入口温度を混合領域の容積Va
パラメータにして求めた結果である。ストラテイ
フイケーシヨンにより死水領域Vbが大きくなる
ほど、即ち、混合領域Vaが小さくなるほど中間
熱交換器入口温度θ*の時間変化は大きく、熱衝撃
が増加する傾向がある。本発明では、第5図に示
したように、一次ナトリウム誘導用円筒18の外
周囲に隙間Bと上下の流入口26,27を有する
ストラテイフイケーシヨン防止用円筒22を設置
したことにより、浮力の影響で上昇した高温ナト
リウムは前述の円筒22の上部から吸込まれ、同
円筒22の下部から流入する低温ナトリウムと混
合するため、第7図のVa/V=1.0の条件を作り
だすことができ、中間熱交換器7の内部構造物へ
の熱衝撃を低減させる事ができる。
θ * =1−Q a /Qe -Qa/QV/Vat* ...(8) However, θ * = (θ p −θ) / (θ p −θ a (O)) ...(9) t * = V/Q FIG. 7 shows the results of determining the intermediate heat exchanger inlet temperature using the volume V a of the mixing region as a parameter when Q a /Q b =1 in equation (8). As the dead water region V b becomes larger due to the strategy, that is, the mixing region V a becomes smaller, the temporal change in the intermediate heat exchanger inlet temperature θ * becomes larger, and thermal shock tends to increase. In the present invention, as shown in FIG. 5, a stratification prevention cylinder 22 having a gap B and upper and lower inflow ports 26 and 27 is installed around the outer periphery of the primary sodium induction cylinder 18, so that the buoyancy The high-temperature sodium that has risen due to the influence of is sucked in from the upper part of the cylinder 22 mentioned above and mixes with the low-temperature sodium flowing in from the lower part of the cylinder 22, so the condition of V a /V = 1.0 in Fig. 7 can be created. , thermal shock to the internal structure of the intermediate heat exchanger 7 can be reduced.

本発明によれば、プラント過度運転時にホツト
プレナム上部に停留する高温ナトリウムと、ホツ
トプレナム下部を流れる低温ナトリウムとを混合
させて中間熱交換器に流入させることができるの
で、中間熱交換器に加わる熱衝撃を小さくするこ
とができる。
According to the present invention, the high-temperature sodium that stays in the upper part of the hot plenum and the low-temperature sodium that flows in the lower part of the hot plenum can be mixed and flowed into the intermediate heat exchanger during excessive plant operation, so that the thermal shock applied to the intermediate heat exchanger is can be made smaller.

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

第1図はタンク型高速炉主容器内の概略構造を
示す側面図、第2図は第1図のA−A断面図、第
3図はプラント過渡時におけるホツトプレナム部
でのナトリウムの流動状況を示す説明図、第4図
は本発明の一実施例を示す側面図、第5図は第4
図に示すホツトプレナム部でのナトリウムの流動
状況を示す説明図、第6図は本発明の効果を説明
するためのホツトプレナム部の簡略図、第7図は
ストラテイフイケーシヨンによつて生じる死水領
域が中間熱交換器入口温度に与える影響を示す線
図である。 1……主容器、2……ルーフスラブ、3……炉
心支持構造物、4……熱遮蔽構造部、5……炉
心、6……炉心上部機構、7……中間熱交換器、
8……1次主循環ポンプ、9……ホツトプレナ
ム、10……コールドプレナム、11……自由液
面、12……補助熱交換器、13……1次ナトリ
ウム流入窓、14……1次ナトリウム流出窓、1
5……下降管、16……2次側下部プレナム、1
7……2次側上部プレナム、18……1次ナトリ
ウム誘導用円筒、19……伝熱管群、23……2
次側出口ノズル。
Figure 1 is a side view showing the schematic structure inside the main vessel of a tank-type fast reactor, Figure 2 is a sectional view taken along line A-A in Figure 1, and Figure 3 shows the sodium flow situation in the hot plenum during plant transition. 4 is a side view showing one embodiment of the present invention, and FIG. 5 is a side view showing an embodiment of the present invention.
Fig. 6 is a simplified diagram of the hot plenum to explain the effects of the present invention, and Fig. 7 shows the dead water area caused by strategy cation. FIG. 3 is a diagram showing the influence on the intermediate heat exchanger inlet temperature. 1... Main vessel, 2... Roof slab, 3... Core support structure, 4... Heat shielding structure, 5... Core, 6... Core upper mechanism, 7... Intermediate heat exchanger,
8...Primary main circulation pump, 9...Hot plenum, 10...Cold plenum, 11...Free liquid level, 12...Auxiliary heat exchanger, 13...Primary sodium inflow window, 14...Primary sodium Outflow window, 1
5...Downcomer pipe, 16...Secondary side lower plenum, 1
7...Secondary side upper plenum, 18...Cylinder for primary sodium induction, 19...Heat transfer tube group, 23...2
Next outlet nozzle.

【特許請求の範囲】[Claims]

1 圧力管型原子炉の圧力管に原子炉の運転に支
障をきたす障害が発生した場合における原子炉の
修復方法であつて、障害を起した圧力管に接続さ
れている入口管の水ドラム近傍および出口管の蒸
気ドラム近傍のそれぞれ適宜個所を切断し、該切
断個所の水ドラム側の入口管端部および蒸気ドラ
ム側の出口管端部に旋栓したのち、前記障害を起
した圧力管をそれに接続している入口管および出
口管からそれぞれ圧力管下部延長部および圧力管
上部上昇管垂直部で切離して該圧力管を引抜き、
外部と連通する冷却材の往復流路とその両端部近
傍に位置する遮蔽プラグとを有する放射線遮蔽用
プラグ管を、前記の引抜いた圧力管の代りに挿入
設置することを特徴とする圧力管型原子炉の修復
方法。
1 A method for repairing a nuclear reactor in the event that a fault occurs in the pressure pipe of a pressure tube reactor that interferes with the operation of the reactor, in which the method is used to repair a nuclear reactor near the water drum of the inlet pipe connected to the faulty pressure pipe. After cutting the outlet pipe at appropriate points near the steam drum and plugging the end of the inlet pipe on the water drum side and the outlet pipe end on the steam drum side at the cut points, the pressure pipe that caused the trouble was removed. pulling out the pressure pipe by disconnecting it from the inlet pipe and outlet pipe connected thereto at the pressure pipe lower extension part and the pressure pipe upper riser pipe vertical part, respectively;
A pressure pipe type characterized in that a radiation shielding plug pipe having a reciprocating coolant flow path communicating with the outside and shielding plugs located near both ends thereof is inserted and installed in place of the pulled out pressure pipe. How to repair a nuclear reactor.

JP56079346A 1981-05-27 1981-05-27 Main container of tank type fast reactor Granted JPS57194387A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56079346A JPS57194387A (en) 1981-05-27 1981-05-27 Main container of tank type fast reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56079346A JPS57194387A (en) 1981-05-27 1981-05-27 Main container of tank type fast reactor

Publications (2)

Publication Number Publication Date
JPS57194387A JPS57194387A (en) 1982-11-29
JPH0151792B2 true JPH0151792B2 (en) 1989-11-06

Family

ID=13687333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56079346A Granted JPS57194387A (en) 1981-05-27 1981-05-27 Main container of tank type fast reactor

Country Status (1)

Country Link
JP (1) JPS57194387A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59126993A (en) * 1983-01-12 1984-07-21 株式会社日立製作所 Tank type fast breeder

Also Published As

Publication number Publication date
JPS57194387A (en) 1982-11-29

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