JP3534591B2 - Method and apparatus for replacing fluid in a spent fuel transport container - Google Patents

Method and apparatus for replacing fluid in a spent fuel transport container

Info

Publication number
JP3534591B2
JP3534591B2 JP30462797A JP30462797A JP3534591B2 JP 3534591 B2 JP3534591 B2 JP 3534591B2 JP 30462797 A JP30462797 A JP 30462797A JP 30462797 A JP30462797 A JP 30462797A JP 3534591 B2 JP3534591 B2 JP 3534591B2
Authority
JP
Japan
Prior art keywords
fluid
spent fuel
replacement
valve
transportation container
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 - Fee Related
Application number
JP30462797A
Other languages
Japanese (ja)
Other versions
JPH11142583A (en
Inventor
光博 入野
量久 田中
俊夫 船越
省三 田口
憲治 邨沢
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP30462797A priority Critical patent/JP3534591B2/en
Publication of JPH11142583A publication Critical patent/JPH11142583A/en
Application granted granted Critical
Publication of JP3534591B2 publication Critical patent/JP3534591B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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

  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、使用済み燃料輸送
容器内の流体、即ちほう酸水の置換方法及び装置に関す
るものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and apparatus for displacing a fluid in a spent fuel transportation container, that is, boric acid water.

【0002】[0002]

【従来の技術】原子力発電プラントにおいて使用済みと
なった燃料集合体は、通常キャスクと呼ばれている使用
済み燃料輸送容器(以下、キャスクともいう)内に収容
され、再処理工場へ輸送される。キャスク内には、使用
済み燃料集合体は発熱し高温でもあり、しかも放射線を
放出するため、その防護のために数1000ppmのほ
う酸水が満たされている。
2. Description of the Related Art A fuel assembly used in a nuclear power plant is housed in a spent fuel transportation container (hereinafter also referred to as a cask) which is usually called a cask, and is transported to a reprocessing plant. . In the cask, the spent fuel assemblies generate heat and are at high temperature, and since they emit radiation, they are filled with several thousand ppm of boric acid water to protect them.

【0003】再処理工場における再処理前に、キャスク
内のほう酸水を排出する必要があるが、排水したほう酸
水の処理設備が再処理工場にない場合には、再処理工場
への輸送前に原子力発電プラント内で純水に置換する必
要があり、しかも、この置換は、対象が放射性であるか
ら効率的に短時間で実施することも重要である。
Before the reprocessing in the reprocessing factory, it is necessary to discharge the boric acid water in the cask. However, if the drainage boric acid water treatment facility is not in the reprocessing factory, before the transportation to the reprocessing factory. It is necessary to replace with pure water in the nuclear power plant, and it is also important to carry out this replacement efficiently and in a short time because the target is radioactive.

【0004】図3の(a)は、従来の混合・希釈による
置換方法の一例を示すもので、キャスク1内に、頂部2
から水を供給して、内部のほう酸水と対流・混合により
希釈してから、底部3から排水し回収している。
FIG. 3 (a) shows an example of a conventional substitution method by mixing / diluting, in which a top portion 2 is provided inside a cask 1.
Water is supplied from the bottom part 3 and diluted with the internal boric acid water by convection and mixing, and then drained from the bottom part 3 and collected.

【0005】[0005]

【発明が解決しようとする課題】しかし、このような方
法では、図3の(b)から分かるように、温度も濃度も
低下が緩慢であり、所望の程度になるまでに長い置換時
間を要するという問題がある。従って、本発明の目的
は、輸送容器の内部流体を比較的に迅速に置換可能な方
法及び装置を提供することである。
However, in such a method, as can be seen from FIG. 3B, both the temperature and the concentration decrease slowly, and a long substitution time is required until the desired degree is reached. There is a problem. Accordingly, it is an object of the present invention to provide a method and apparatus that allows the fluid inside a shipping container to be replaced relatively quickly.

【0006】[0006]

【課題を解決するための手段】この目的から、請求項1
に係る本発明によると、内部流体を含む使用済み燃料輸
送容器の鉛直方向下部から、前記内部流体よりも相対的
に低温の流体を注入して、前記内部流体及び前記注入さ
れた低温流体の間に成層界面を形成し、該成層界面の上
下にある前記内部流体及び前記低温流体間の密度差に起
因する同成層界面の上昇効果により、前記内部流体を前
記注入流体と置換する使用済み燃料輸送容器内の流体の
置換方法を提供している。
To this end, claim 1
According to the present invention, a fluid having a temperature relatively lower than that of the internal fluid is injected from a vertically lower portion of the spent fuel transportation container containing the internal fluid, and the fluid is injected between the internal fluid and the injected cryogenic fluid. A spent fuel transport that forms a stratified interface in the inner layer and replaces the internal fluid with the injected fluid by the ascending effect of the stratified interface due to the density difference between the internal fluid and the cryogenic fluid above and below the stratified interface. A method of replacing a fluid in a container is provided.

【0007】また、この目的を達成するため、請求項2
に係る本発明では、下部にドレンバルブを有し上部にベ
ントバルブ及び加圧バルブを有する使用済み燃料輸送容
器内の内部流体を、該内部流体より相対的に低温の置換
流体と置換するための装置は、前記置換流体を貯留する
ための貯留タンクと、該貯留タンクを前記使用済み燃料
輸送容器の前記ドレンバルブに接続する置換流体供給ラ
インと、同置換流体供給ラインに介装されて前記貯留タ
ンク内の前記置換流体を前記使用済み燃料輸送容器に送
給するポンプと、前記使用済み燃料輸送容器の前記ベン
トバルブ及び前記加圧バルブに接続され前記内部流体を
外部に排出するための排出ラインと、該排出ラインに接
続された回収タンクとを備えている。
Further, in order to achieve this object, claim 2
In the present invention according to, for replacing the internal fluid in the spent fuel transportation container having the drain valve in the lower part and the vent valve and the pressurizing valve in the upper part with the replacement fluid having a relatively lower temperature than the internal fluid, The apparatus includes a storage tank for storing the replacement fluid, a replacement fluid supply line connecting the storage tank to the drain valve of the spent fuel transportation container, and the storage tank interposed in the replacement fluid supply line. A pump for feeding the replacement fluid in the tank to the spent fuel transportation container, and a discharge line for discharging the internal fluid to the outside, which is connected to the vent valve and the pressure valve of the spent fuel transportation container. And a recovery tank connected to the discharge line.

【0008】[0008]

【発明の実施の形態】次に、本発明の好適な実施形態に
ついて添付図面を参照して詳細に説明するが、図中、同
一符号は同一又は相当部分を示すものとする。図1にお
いて、使用済み燃料輸送容器10自体は周知の構造のも
のでよいので簡単に説明すると、筒状の遮蔽層11と、
その周りを囲む放熱フィン集合体12とを備え、遮蔽層
11の頂部及び底部は上部及び下部の蓋組立体13,1
4により封止されている。遮蔽層11の内部には、各燃
料集合体15を縦に収納する複数のチャンネル16が垂
設されており、該チャンネル16を軸方向に離間して多
数設けられた支持リング17により支持している。
BEST MODE FOR CARRYING OUT THE INVENTION Next, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the drawings, the same reference numerals indicate the same or corresponding parts. In FIG. 1, since the spent fuel transportation container 10 itself may have a well-known structure, it will be briefly described.
And a heat dissipation fin assembly 12 surrounding it, and the top and bottom of the shielding layer 11 are upper and lower lid assemblies 13, 1.
It is sealed by 4. A plurality of channels 16 for vertically accommodating each fuel assembly 15 are vertically provided inside the shielding layer 11, and the channels 16 are supported by a large number of support rings 17 which are axially separated from each other. There is.

【0009】また、輸送容器10には、その内部の流体
を排出するために、下部蓋組立体14にドレンバルブ2
6が設けられており、上部蓋組立体13には、流体レベ
ルを調節するためにベントバルブ29が設けられ、流体
が沸騰しないように加圧ガスを注入するために加圧バル
ブ30が設けられている。置換前、この輸送容器10内
には100℃以下の数1000ppm濃度のほう酸水
(図示せず)が満たされている。本発明の置換方法及び
装置は、輸送容器10内の高温・高濃度のほう酸水を効
率よく純水と置換するものである。
Further, the drain valve 2 is attached to the lower lid assembly 14 of the transport container 10 in order to discharge the fluid therein.
6 is provided, the upper lid assembly 13 is provided with a vent valve 29 for adjusting the fluid level, and a pressurizing valve 30 for injecting pressurized gas so that the fluid does not boil. ing. Before the replacement, the transportation container 10 is filled with boric acid water (not shown) having a concentration of several 1000 ppm at 100 ° C. or less. INDUSTRIAL APPLICABILITY The replacement method and apparatus of the present invention efficiently replace high temperature and high concentration boric acid water in the transportation container 10 with pure water.

【0010】図1において、流体の置換装置もしくはシ
ステム20は、純水を輸送容器10内に供給するため、
輸送容器に見合う容量の純水タンク21を備え、また、
該輸送容器10から回収したほう酸水を収容するため、
同様の容量の回収タンク22を備えている。純水タンク
21は、純水供給ポンプ23及び適宜のバルブ24を含
む純水供給ライン25により輸送容器10の内部に下部
蓋組立体14からドレンバルブ26を介して流体連通し
ており、回収タンク22は、バルブ27を含む排水ライ
ン28により輸送容器10の内部に上部蓋組立体13か
らベントバルブ29を介して流体連通している。また、
回収タンク22に連通する排水ライン28は、バルブ3
1を介して前述した加圧バルブ30にも連通している。
In FIG. 1, the fluid displacement device or system 20 supplies pure water into the transport container 10,
It is equipped with a pure water tank 21 of a capacity suitable for the transport container,
In order to accommodate the boric acid water recovered from the transport container 10,
The recovery tank 22 having the same capacity is provided. The pure water tank 21 is in fluid communication with the pure water supply line 25 including the pure water supply pump 23 and an appropriate valve 24 from the lower lid assembly 14 to the inside of the transportation container 10 through the drain valve 26. 22 is in fluid communication with the interior of the shipping container 10 from the upper lid assembly 13 via a vent valve 29 by a drain line 28 including a valve 27. Also,
The drainage line 28 communicating with the recovery tank 22 includes the valve 3
It communicates also with the pressurizing valve 30 mentioned above via 1.

【0011】この流体置換システム20において、各バ
ルブを開いて純水供給ポンプ23を作動すれば、純水タ
ンク21の純水が純水供給ライン25を介して輸送容器
10内に注入され、内部のほう酸水は、ベントバルブ2
9を含む水位調整ラインとバルブ30,31を含む加圧
ラインとからなる排水ライン28を介して浮力効果によ
り回収タンク22に回収される。
In this fluid displacement system 20, when each valve is opened and the pure water supply pump 23 is operated, the pure water in the pure water tank 21 is injected into the transportation container 10 through the pure water supply line 25, and the inside The boric acid water is vent valve 2
The water is recovered in the recovery tank 22 by the buoyancy effect via the drain line 28 including the water level adjusting line including 9 and the pressurizing line including the valves 30 and 31.

【0012】図2の(a)は、この浮力効果について説
明するための図である。置換プロセスの開始時には、輸
送容器10内には高温のほう酸水が充満しているため、
水の比重量は小さくなっている。そのような状況下で、
ベントバルブ29及び加圧バルブ30を開成すると共
に、輸送容器10の下部にあるドレンバルブ26から相
対的に低温の純水(比重量が大きい)を注入すると、比
重の違いにより、注入純水PWと高温ほう酸水BWの境
界に成層界面Aが形成される。この成層界面Aの近傍で
は、熱の授受は生じているが、成層界面自体は、純水の
注入進行に連れて図2の(a)に符号A’,A”で示す
ように徐々に上昇し、全体的には、あたかもピストンが
動くように流れるピストンフローを形成する。
FIG. 2A is a diagram for explaining this buoyancy effect. At the start of the replacement process, the shipping container 10 is full of hot boric acid water,
The specific weight of water is small. Under such circumstances,
When the vent valve 29 and the pressurizing valve 30 are opened and pure water of relatively low temperature (large specific weight) is injected from the drain valve 26 at the bottom of the transport container 10, the injected pure water PW is generated due to the difference in specific gravity. A stratified interface A is formed at the boundary between the high temperature boric acid water BW and the high temperature boric acid water BW. Although heat is exchanged in the vicinity of the stratified interface A, the stratified interface itself gradually rises as indicated by symbols A ′ and A ″ in FIG. However, as a whole, it forms a piston flow that flows as if the piston were moving.

【0013】従って、下方からの純水PWにより、上方
の高温ほう酸水BWは輸送容器10から押し出され、ベ
ントバルブ29及び加圧バルブ30を介して図1の回収
タンク22に排水される。
Therefore, the high temperature boric acid water BW in the upper part is pushed out of the transport container 10 by the pure water PW from the lower part and is drained to the recovery tank 22 in FIG. 1 through the vent valve 29 and the pressurizing valve 30.

【0014】このような本発明の置換方式によると、輸
送容器の高さ方向のある位置を成層界面が通過すると、
その位置近傍での温度,濃度は急激に低下するため、図
2の(b)から了解されるように、図3の(b)の従来
例と比較して、置換に要する時間が大幅に短縮できる。
According to such a substitution system of the present invention, when the stratified interface passes through a certain position in the height direction of the transportation container,
Since the temperature and the concentration in the vicinity of that position drop sharply, as can be understood from FIG. 2B, the time required for replacement is significantly shortened as compared with the conventional example of FIG. 3B. it can.

【0015】以上、本発明をその好適な実施形態につい
て説明したが、本発明はこれに限定されるものではな
く、例えば次のような様々な改変が可能である。 1)輸送容器の内部流体は、濃度数1000ppmのほ
う酸水としたが、冷却・制御機能があれば濃度を含めて
任意の流体でよく、また、置換流体も純水に限らない。 2)輸送容器に備わっているドレンバルブとベントバル
ブ及び加圧バルブとを置換流体の注入と内部流体の排出
とにそれぞれ用いることがコスト上有利であるため、実
施形態ではそのように構成したが、本発明が適用される
輸送容器の形態に応じて、例えば、ドレンバルブとベン
トバルブ及び加圧バルブとに対応するものを用いたり、
対応するものが存在しなければ、別に弁装置を設置して
もよい。 3)また、内部流体の排出には、ベントバルブ及び加圧
バルブの双方を用いることが好適ではあるが、用いるこ
とが必須ではなく、どちらか一方を用いるだけでもよ
い。 4)実施形態では使用済み燃料は燃料集合体であるが、
輸送容器内の流体の置換が必要である限り、使用済み燃
料がその他の燃料、放射性物質もしくは放射性廃棄物の
ようなものでもよい。
Although the present invention has been described above with reference to its preferred embodiment, the present invention is not limited to this, and various modifications such as the following are possible. 1) The internal fluid of the transportation container is boric acid water having a concentration of 1000 ppm, but any fluid including the concentration may be used as long as it has a cooling / control function, and the replacement fluid is not limited to pure water. 2) Since it is cost effective to use the drain valve, the vent valve, and the pressurizing valve, which are provided in the transport container, for injecting the replacement fluid and discharging the internal fluid, the embodiment has such a configuration. Depending on the form of the transportation container to which the present invention is applied, for example, those corresponding to the drain valve, the vent valve and the pressurizing valve may be used,
If no counterpart exists, a separate valve device may be installed. 3) Although it is preferable to use both the vent valve and the pressurizing valve for discharging the internal fluid, it is not essential to use them, and only one of them may be used. 4) In the embodiment, the spent fuel is a fuel assembly,
The spent fuel may be other fuels, radioactive material or radioactive waste, as long as the fluid in the shipping container needs to be replaced.

【0016】[0016]

【発明の効果】以上のように、請求項1に係る方法発明
では、内部流体を含む使用済み燃料輸送容器の鉛直方向
下部から、前記内部流体よりも相対的に低温の流体を注
入して、前記内部流体及び前記注入された低温流体の間
に成層界面を形成し、該成層界面の上下にある前記内部
流体及び前記低温流体間の密度差に起因する同成層界面
の上昇効果により、前記内部流体を前記注入流体と置換
しており、請求項2に係る装置発明では、下部にドレン
バルブを有し上部にベントバルブ及び加圧バルブを有す
る使用済み燃料輸送容器内の内部流体を、該内部流体よ
り相対的に低温の置換流体と置換するための装置は、前
記置換流体を貯留するための貯留タンクと、該貯留タン
クを前記使用済み燃料輸送容器の前記ドレンバルブに接
続する置換流体供給ラインと、同置換流体供給ラインに
介装されて前記貯留タンク内の前記置換流体を前記使用
済み燃料輸送容器に送給するポンプと、前記使用済み燃
料輸送容器の前記ベントバルブ及び前記加圧バルブに接
続され前記内部流体を外部に排出するための排出ライン
と、該排出ラインに接続された回収タンクとを備えてい
る。そのため、請求項1及び請求項2の発明では、相対
的に低温の置換流体が輸送容器の下部から注入され、輸
送容器の内部流体が上部から排出されるので、輸送容器
内においては、下方の置換流体と上方の内部流体との間
に浮力効果もしくは密度差効果による成層界面が形成さ
れる。この成層界面は、置換流体の注入を続けることに
より、徐々に上昇する。成層界面の上下では両流体間に
大きな温度差、延いては大きな濃度差が生じるため、複
雑な内部構造の輸送容器であっても、その内部流体を置
換流体と相対的に短時間で置換することができる。ま
た、成層界面が上述のように上昇するピストンフローの
効果により、輸送容器内を効果的に除染することもでき
る。
As described above, in the method invention according to claim 1, a fluid having a temperature relatively lower than that of the internal fluid is injected from the vertically lower portion of the spent fuel transportation container containing the internal fluid, A stratified interface is formed between the internal fluid and the injected low temperature fluid, and the internal layer is increased due to a difference in density between the internal fluid and the low temperature fluid above and below the stratified interface. In the device invention according to claim 2, the fluid is replaced with the injected fluid, and the internal fluid in the spent fuel transportation container having the drain valve in the lower portion and the vent valve and the pressurizing valve in the upper portion is An apparatus for replacing a replacement fluid having a temperature relatively lower than that of a fluid includes a storage tank for storing the replacement fluid and a replacement fluid supply connecting the storage tank to the drain valve of the spent fuel transportation container. A line, a pump interposed in the replacement fluid supply line for feeding the replacement fluid in the storage tank to the spent fuel transport container, the vent valve and the pressurization valve of the spent fuel transport container And a recovery tank connected to the exhaust line for exhausting the internal fluid to the outside, and a recovery tank connected to the exhaust line. Therefore, in the inventions of claims 1 and 2, the relatively low-temperature substitution fluid is injected from the lower portion of the transportation container, and the internal fluid of the transportation container is discharged from the upper portion. A stratified interface is formed between the displacement fluid and the internal fluid above due to the buoyancy effect or the density difference effect. This stratified interface gradually rises by continuing the injection of the displacement fluid. Since there is a large temperature difference between the two fluids above and below the stratified interface, and consequently a large concentration difference, even in a transport container with a complicated internal structure, the internal fluid is replaced with the replacement fluid in a relatively short time. be able to. Further, the inside of the transport container can be effectively decontaminated by the effect of the piston flow in which the stratified interface rises as described above.

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

【図1】 本発明の一実施形態に係る置換方法とその実
施のための置換装置とを説明する系統図である。
FIG. 1 is a system diagram illustrating a replacement method and a replacement device for carrying out the replacement method according to an embodiment of the present invention.

【図2】 (a)は、本発明に従って浮力効果により生
ずるピストンフローを説明するための略図、(b)は、
ピストンフローが生じている輸送容器内の特定部位の温
度・濃度変化を示すグラフである。
FIG. 2 (a) is a schematic diagram for explaining a piston flow caused by a buoyancy effect according to the present invention, and FIG.
It is a graph which shows temperature / concentration change of a specific part in a transportation container in which a piston flow has occurred.

【図3】 (a)は、従来の混合希釈方式を説明するた
めの略図、(b)は、その混合希釈方式を実施した場合
の輸送容器内の特定部位の温度・濃度変化を示すグラフ
である。
FIG. 3 (a) is a schematic diagram for explaining a conventional mixed dilution method, and FIG. 3 (b) is a graph showing changes in temperature / concentration of a specific portion in a transportation container when the mixed dilution method is performed. is there.

【符号の説明】[Explanation of symbols]

10…使用済み燃料輸送容器、15…燃料集合体(使用
済み燃料)、20…置換装置もしくはシステム、21…
純水タンク(貯留タンク)、22…回収タンク、23…
純水供給ポンプ、25…純水供給ライン(置換流体供給
ライン)、26…ドレンバルブ、28…排水ライン(排
出ライン)、29…ベントバルブ、30…加圧バルブ、
A…成層界面、PW…純水(置換流体)、BW…ほう酸
水(内部流体)。
10 ... Spent fuel transportation container, 15 ... Fuel assembly (spent fuel), 20 ... Replacement device or system, 21 ...
Pure water tank (storage tank), 22 ... Recovery tank, 23 ...
Pure water supply pump, 25 ... Pure water supply line (displacement fluid supply line), 26 ... Drain valve, 28 ... Drain line (discharge line), 29 ... Vent valve, 30 ... Pressurization valve,
A ... Stratified interface, PW ... Pure water (displacement fluid), BW ... Boric acid water (internal fluid).

───────────────────────────────────────────────────── フロントページの続き (72)発明者 田口 省三 兵庫県神戸市兵庫区和田崎町一丁目1番 1号 三菱重工業株式会社 神戸造船所 内 (72)発明者 邨沢 憲治 兵庫県神戸市兵庫区和田崎町一丁目1番 1号 三菱重工業株式会社 神戸造船所 内 (56)参考文献 特開 平9−80196(JP,A) 特開 平9−197083(JP,A) (58)調査した分野(Int.Cl.7,DB名) G21C 19/32 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Shozo Taguchi 1-1-1, Wadazaki-cho, Hyogo-ku, Kobe-shi, Hyogo Mitsubishi Heavy Industries, Ltd. Kobe Shipyard (72) Inventor Kenji Usawa Kobe-shi, Hyogo 1-1 1-1 Wadasaki-cho, Hyogo-ku Mitsubishi Heavy Industries, Ltd. Kobe Shipyard (56) References Japanese Patent Laid-Open No. 9-80196 (JP, A) Japanese Patent Laid-Open No. 9-197083 (JP, A) (58) Survey Areas (Int.Cl. 7 , DB name) G21C 19/32

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 内部流体を含む使用済み燃料輸送容器の
鉛直方向下部から、前記内部流体よりも相対的に低温の
流体を注入して、前記内部流体及び前記注入された低温
流体の間に成層界面を形成し、該成層界面の上下にある
前記内部流体及び前記低温流体間の密度差に起因する同
成層界面の上昇効果により、前記内部流体を前記注入流
体と置換する使用済み燃料輸送容器内の流体の置換方
法。
1. A stratification between the internal fluid and the injected cryogenic fluid by injecting a fluid having a temperature relatively lower than that of the internal fluid from a vertically lower portion of a spent fuel transportation container containing the internal fluid. A spent fuel transport container that forms an interface and replaces the internal fluid with the injected fluid by the ascending effect of the stratified interface due to the density difference between the internal fluid and the cryogenic fluid above and below the stratified interface. Fluid replacement method.
【請求項2】 下部にドレンバルブを有し上部にベント
バルブ及び加圧バルブを有する使用済み燃料輸送容器内
の内部流体を、該内部流体より相対的に低温の置換流体
と置換するための装置であって、前記置換流体を貯留す
るための貯留タンクと、該貯留タンクを前記使用済み燃
料輸送容器の前記ドレンバルブに接続する置換流体供給
ラインと、同置換流体供給ラインに介装されて前記貯留
タンク内の前記置換流体を前記使用済み燃料輸送容器に
送給するポンプと、前記使用済み燃料輸送容器の前記ベ
ントバルブ及び前記加圧バルブに接続され前記内部流体
を外部に排出するための排出ラインと、該排出ラインに
接続された回収タンクとを備える使用済み燃料輸送容器
内の流体の置換装置。
2. An apparatus for replacing an internal fluid in a spent fuel transportation container having a drain valve at a lower portion and a vent valve and a pressurizing valve at an upper portion with a replacement fluid having a temperature lower than that of the internal fluid. A storage tank for storing the replacement fluid, a replacement fluid supply line connecting the storage tank to the drain valve of the spent fuel transport container, and the replacement fluid supply line interposed therebetween. A pump for supplying the replacement fluid in the storage tank to the spent fuel transportation container, and a discharge for discharging the internal fluid to the outside, which is connected to the vent valve and the pressurization valve of the spent fuel transportation container. A device for displacing a fluid in a spent fuel transportation container, comprising a line and a recovery tank connected to the discharge line.
JP30462797A 1997-11-06 1997-11-06 Method and apparatus for replacing fluid in a spent fuel transport container Expired - Fee Related JP3534591B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30462797A JP3534591B2 (en) 1997-11-06 1997-11-06 Method and apparatus for replacing fluid in a spent fuel transport container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30462797A JP3534591B2 (en) 1997-11-06 1997-11-06 Method and apparatus for replacing fluid in a spent fuel transport container

Publications (2)

Publication Number Publication Date
JPH11142583A JPH11142583A (en) 1999-05-28
JP3534591B2 true JP3534591B2 (en) 2004-06-07

Family

ID=17935316

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30462797A Expired - Fee Related JP3534591B2 (en) 1997-11-06 1997-11-06 Method and apparatus for replacing fluid in a spent fuel transport container

Country Status (1)

Country Link
JP (1) JP3534591B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009258096A (en) * 2008-03-19 2009-11-05 Mitsubishi Heavy Ind Ltd Cask-cleaning apparatus and cask-cleaning method

Also Published As

Publication number Publication date
JPH11142583A (en) 1999-05-28

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