JPH1114795A - Decontaminating method for reactor pressure vessel - Google Patents
Decontaminating method for reactor pressure vesselInfo
- Publication number
- JPH1114795A JPH1114795A JP16590497A JP16590497A JPH1114795A JP H1114795 A JPH1114795 A JP H1114795A JP 16590497 A JP16590497 A JP 16590497A JP 16590497 A JP16590497 A JP 16590497A JP H1114795 A JPH1114795 A JP H1114795A
- Authority
- JP
- Japan
- Prior art keywords
- pressure vessel
- reactor pressure
- decontamination
- pump
- reactor
- 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.)
- Granted
Links
Landscapes
- Cleaning By Liquid Or Steam (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は原子力発電所におい
て、原子炉圧力容器内の化学除染作業時の除染液の流速
を確保し、所定の流量に制御して化学除染を効率的に行
うことができる原子炉圧力容器内の除染方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a nuclear power plant, in which a flow rate of a decontamination solution during a chemical decontamination operation in a reactor pressure vessel is secured, and a predetermined flow rate is controlled to efficiently perform chemical decontamination. The present invention relates to a decontamination method in a reactor pressure vessel that can be performed.
【0002】[0002]
【従来の技術】原子力発電所においては炉水中放射能が
機器や配管の表面の酸化皮膜中に取り込まれて被曝線源
になるため、保守、点検、補修期間の前にこの放射能を
除去する方策が採られている。その一つに化学除染技術
が知られている。2. Description of the Related Art In a nuclear power plant, radioactivity in reactor water is taken into an oxide film on the surface of equipment and piping and becomes a radiation source. Therefore, this radioactivity is removed before maintenance, inspection, and repair. Measures have been taken. One of them is a chemical decontamination technique.
【0003】従来はポンプケーシング,インペラ,弁な
どの機器単体、原子炉再循環系、原子炉浄化系などの系
統に対して行われている。しかし、原子炉圧力容器内の
補修作業を行うにあたり、どうしても遠隔、自動で実施
できない部位については人手に頼らざるを得ない場合が
あり、原子炉圧力容器内全域にわたり除染が必要となっ
ている。[0003] Conventionally, this is performed for systems such as pump casings, impellers, valves, and other equipment alone, a reactor recirculation system, and a reactor purification system. However, when performing repair work inside the reactor pressure vessel, it may be necessary to rely on humans for parts that cannot be performed remotely and automatically, and decontamination is required throughout the reactor pressure vessel. .
【0004】[0004]
【発明が解決しようとする課題】従来、原子炉圧力容器
内においては原子炉圧力容器の内壁面などをジェット洗
浄などの機械方式によって除染を行っているが、機械的
な除染方法ではあまり高い除染効果は望めないうえに、
長時間を要するという課題がある。Conventionally, in the reactor pressure vessel, decontamination of the inner wall surface of the reactor pressure vessel and the like has been performed by a mechanical method such as jet cleaning, but the mechanical decontamination method is not so common. A high decontamination effect cannot be expected,
There is a problem that it takes a long time.
【0005】また、原子炉圧力容器内の化学除染を効果
的に行う場合、除染液に浸漬させておくだけでなく、除
染に必要な炉内流動を確保するため、原子炉再循環系
(PLR)ポンプを運転するという方法が考えられる。In order to effectively perform chemical decontamination in the reactor pressure vessel, not only is it immersed in the decontamination solution, but also the reactor is recirculated in order to secure the necessary reactor flow for decontamination. A method of operating a system (PLR) pump is conceivable.
【0006】後者の場合、原子炉圧力容器内から燃料集
合体および制御棒を取り出した状態で再循環ポンプを通
常通り運転すれば過剰流量となる。また、再循環ポンプ
の運転に伴いシール水を供給することが必要になるた
め、原子炉圧力容器から溢れることを防止するなんらか
の措置を取る必要がある。さらに、水位が低いままの状
態で運転すると原子炉圧力容器の内壁面を除染すること
ができないため、原子炉圧力容器内の放射線量を十分に
低減できない課題がある。In the latter case, if the recirculation pump is operated as usual with the fuel assemblies and control rods taken out of the reactor pressure vessel, an excessive flow rate will result. In addition, since it is necessary to supply seal water with the operation of the recirculation pump, it is necessary to take some measures to prevent overflow from the reactor pressure vessel. Furthermore, when the operation is performed with the water level kept low, the inner wall surface of the reactor pressure vessel cannot be decontaminated, so that there is a problem that the radiation dose in the reactor pressure vessel cannot be sufficiently reduced.
【0007】本発明は上記課題を解決するためになされ
たもので、原子炉圧力容器内の化学除染時に再循環ポン
プを運転して除染に必要な流速を確保し、除染液が浸ら
ないか、または浸る時間の短い原子炉圧力容器内壁面に
除染液を供給して原子炉圧力容器内の除染液流量を所定
の値に制御し、化学除染を効率的に行うことができ、そ
の結果として作業員の放射線被曝を低減することができ
る原子炉圧力容器内の除染方法およびその除染装置を提
供することにある。SUMMARY OF THE INVENTION The present invention has been made to solve the above problems, and operates a recirculation pump during chemical decontamination in a reactor pressure vessel to secure a flow rate necessary for decontamination and to soak the decontamination liquid. The decontamination solution is supplied to the inner surface of the reactor pressure vessel where there is no or short immersion time, and the flow rate of the decontamination solution in the reactor pressure vessel is controlled to a predetermined value to enable efficient chemical decontamination. It is an object of the present invention to provide a decontamination method and a decontamination apparatus in a reactor pressure vessel that can reduce radiation exposure of workers as a result.
【0008】[0008]
【課題を解決するための手段】請求項1の発明は、原子
炉圧力容器内に設置されたシュラウドとの間に炉水を強
制循環させるジェットポンプが設けられ、このジェット
ポンプからの炉水を前記原子炉圧力容器の下部外面に接
続した再循環系入口ノズルおよび出口ノズルを通して循
環させる再循環系配管および再循環ポンプが設けられ、
この再循環ポンプの駆動により前記原子炉圧力容器内に
供給した除染液に流動を付与する原子炉圧力容器内の化
学除染方法において、前記原子炉圧力容器内の底部また
は前記ジェットポンプの底部近傍に流す除染液の流速を
少なくとも1cm/秒に選定して前記除染液に流動を付与
することを特徴とする。According to a first aspect of the present invention, there is provided a jet pump for forcibly circulating reactor water with a shroud installed in a reactor pressure vessel, and the reactor water from the jet pump is provided. A recirculation pipe and a recirculation pump that circulate through a recirculation system inlet nozzle and an outlet nozzle connected to a lower outer surface of the reactor pressure vessel are provided,
In the chemical decontamination method in a reactor pressure vessel for applying a flow to the decontamination liquid supplied into the reactor pressure vessel by driving the recirculation pump, the bottom in the reactor pressure vessel or the bottom of the jet pump The flow rate of the decontamination liquid flowing in the vicinity is selected to be at least 1 cm / sec, and the decontamination liquid is provided with a flow.
【0009】請求項1の発明によれば、原子炉圧力容器
内の除染液滞留部または低流速部となる原子炉圧力容器
内底部またはジェットポンプ底部近傍の流速を少なくと
も1cm/秒とすることにより、当該部における除染効率
を高めることができる。なお、除染液の流速を少なくと
も1cm/秒に選定した理由は図1に示すように実験結果
に基づくものである。According to the first aspect of the present invention, the flow velocity in the vicinity of the bottom of the reactor pressure vessel or the bottom of the jet pump, which is the decontamination liquid retention section or the low flow rate section in the reactor pressure vessel, is at least 1 cm / sec. Thereby, the decontamination efficiency in the part can be increased. The reason why the flow rate of the decontamination solution was selected to be at least 1 cm / sec is based on experimental results as shown in FIG.
【0010】請求項2の発明は、前記再循環ポンプを定
格運転時の20%から30%の回転数で運転して前記除染液
に流動を付与することを特徴とする。請求項2の発明に
よれば、少なくとも1cm/秒の流速を得るためには再循
環ポンプを定格運転時の20〜30%の回転数に選定する。
この20%未満では所定の流速、つまり1cm/秒以上の流
速を得ることができないため、除染に必要な流動が確保
できない。一方、30%を超えると、再循環ポンプのシー
ル水が必要以上に多く流れ込むことになって除染液が希
薄となり、除染効率が低下するだけでなく、過剰流量と
なって原子炉圧力容器から溢れ出すことになるので不可
である。[0010] The invention of claim 2 is characterized in that the recirculation pump is operated at a rotation speed of 20% to 30% of the rated operation to impart a flow to the decontamination liquid. According to the second aspect of the invention, in order to obtain a flow rate of at least 1 cm / sec, the recirculation pump is selected to have a rotation speed of 20 to 30% of the rated operation.
If the flow rate is less than 20%, a predetermined flow rate, that is, a flow rate of 1 cm / sec or more cannot be obtained, so that a flow required for decontamination cannot be secured. On the other hand, if it exceeds 30%, the sealing water of the recirculation pump will flow more than necessary and the decontamination solution will be diluted, which will not only reduce the decontamination efficiency, but also increase the flow rate of the reactor pressure vessel. It is impossible because it overflows from the.
【0011】請求項3の発明は、原子炉圧力容器内の底
部または前記原子炉圧力容器内に設置されたジェットポ
ンプの底部近傍に仮設水中ポンプを吊り降ろして前記水
中ポンプの駆動により前記除染液に流動を付与すること
を特徴とする。According to a third aspect of the present invention, a temporary submersible pump is suspended at the bottom of the reactor pressure vessel or near the bottom of the jet pump installed in the reactor pressure vessel, and the decontamination is performed by driving the submersible pump. It is characterized in that a fluid is imparted to the liquid.
【0012】請求項3の発明によれば、仮設水中ポンプ
を設置することにより、原子炉圧力容器内の除染液滞留
部または低流速部となっている原子炉圧力容器内底部ま
たはジェットポンプ底部近傍の除染液の流速を1cm/秒
以上に確保できる。According to the third aspect of the present invention, by installing a temporary submersible pump, the bottom of the reactor pressure vessel or the bottom of the jet pump which is a decontamination liquid stagnation section or a low flow rate section in the reactor pressure vessel. The flow rate of the decontamination solution in the vicinity can be maintained at 1 cm / sec or more.
【0013】請求項4の発明は、原子炉圧力容器内底部
から貫通して林立する複数の制御棒駆動機構案内管の上
端開口にキャップを被せて前記原子炉圧力容器底部の除
染液の流動を促進させることを特徴とする。According to a fourth aspect of the present invention, a flow of the decontamination liquid at the bottom of the reactor pressure vessel is provided by capping the upper end opening of a plurality of control rod drive mechanism guide tubes penetrating from the bottom of the reactor pressure vessel. Is promoted.
【0014】請求項4の発明によれば、原子炉圧力容器
内底部に突設している制御棒駆動機構案内管にキャップ
を被せることにより、除染液の流れを分散させ原子炉圧
力容器内中心部近傍から底部に均一に除染効率が得られ
る流速をいきとどかせて、除染液の流動性を向上させる
ことにより請求項1の条件を達成できる。According to the fourth aspect of the present invention, the control rod drive mechanism guide tube protruding from the bottom of the reactor pressure vessel is covered with a cap, thereby dispersing the flow of the decontamination liquid and allowing the decontamination liquid to flow inside the reactor pressure vessel. The condition of claim 1 can be achieved by increasing the flow rate at which decontamination efficiency can be uniformly obtained from the vicinity of the center to the bottom to improve the fluidity of the decontamination liquid.
【0015】請求項5の発明は、原子炉圧力容器内の底
部または前記ジェットポンプの底部に回転体を設けて前
記各底部の除染液の撹拌を促進することを特徴とする。
請求項5の発明によれば、原子炉圧力容器内の除染液滞
留部または低流速部となっている原子炉圧力容器の底
部、またはジェットポンプの底部近傍の除染液を仮設回
転体の駆動により撹拌し、除染液の流速を確保して請求
項1の条件を達成できる。[0015] The invention of claim 5 is characterized in that a rotating body is provided at the bottom of the reactor pressure vessel or at the bottom of the jet pump to promote agitation of the decontamination liquid at each of the bottoms.
According to the invention of claim 5, the decontamination liquid in the vicinity of the bottom of the reactor pressure vessel or the bottom of the jet pump, which is a decontamination liquid stagnation section or a low flow rate section in the reactor pressure vessel, is supplied to the temporary rotating body. The condition of claim 1 can be achieved by stirring by driving to secure the flow rate of the decontamination liquid.
【0016】請求項6の発明は、原子炉圧力容器内の中
央部に大径仮設タンクを設置して前記原子炉圧力容器底
部の除染液の流動性を向上させることを特徴とする。請
求項6の発明によれば、原子炉圧力容器内にタンクを障
害物として設置し、再循環ポンプの少ない回転数で除染
液滞留部または低流速部となっている原子炉圧力容器内
底部の除染液流動性を向上させ、請求項1の条件を達成
できる。A sixth aspect of the present invention is characterized in that a large-diameter temporary tank is installed at the center of the reactor pressure vessel to improve the flowability of the decontamination liquid at the bottom of the reactor pressure vessel. According to the invention of claim 6, the tank is installed as an obstacle in the reactor pressure vessel, and the bottom portion of the reactor pressure vessel which serves as a decontamination liquid stagnation section or a low flow rate section with a small number of rotations of the recirculation pump. Can improve the fluidity of the decontamination liquid, and can achieve the conditions of claim 1.
【0017】請求項7の発明は、前記原子炉圧力容器内
の機械的除染機能を併用することを特徴とする。請求項
7の発明によれば、原子炉圧力容器内の底部やジェット
ポンプ底部に1cm/秒以上の流速が確保できない場合、
機械的洗浄を併用することにより除染効果を高めること
ができる。すなわち、除染剤に放射能が十分溶解せず、
スラッジとして堆積するのを機械除染の併用により系外
に排出することで、除染効果を向上させることができ
る。A seventh aspect of the present invention is characterized in that a mechanical decontamination function in the reactor pressure vessel is used together. According to the invention of claim 7, when a flow rate of 1 cm / sec or more cannot be secured at the bottom in the reactor pressure vessel or the jet pump bottom,
By using mechanical cleaning together, the decontamination effect can be enhanced. That is, radioactivity is not sufficiently dissolved in the decontamination agent,
The decontamination effect can be improved by discharging the sludge deposited outside the system in combination with mechanical decontamination.
【0018】請求項8の発明は、原子炉圧力容器内の底
部または前記ジェットポンプ底部に除染液の流動を促進
する除染液の出口または入口あるいはその両者を設ける
ことを特徴とする。An eighth aspect of the present invention is characterized in that a decontamination liquid outlet and / or an inlet for promoting the flow of the decontamination liquid are provided at the bottom of the reactor pressure vessel or at the bottom of the jet pump.
【0019】請求項8の発明によれば、原子炉圧力容器
内の除染液滞留部または低流速部となっている原子炉圧
力容器内の底部またはジェットポンプ底部近傍の除染液
流速を確保するために、当該部に除染液の吸い込み口ま
たは吐き出し口あるいはその両者を設けることにより請
求項1の条件を達成することができる。According to the eighth aspect of the present invention, the flow rate of the decontamination liquid in the vicinity of the bottom of the reactor pressure vessel or the bottom of the jet pump, which is the detention section of the decontamination liquid in the reactor pressure vessel or the low flow rate section, is ensured. In order to achieve this, the condition of claim 1 can be achieved by providing a suction port and / or a discharge port for the decontamination liquid in the section.
【0020】請求項9の発明は、原子炉圧力容器内の底
部または前記ジェットポンプの底部近傍に気泡発生口を
設けて除染液の流動を促進することを特徴とする。請求
項9の発明によれば、原子炉圧力容器内の除染液滞留部
または低流速部となっている原子炉圧力容器内の底部、
ジェットポンプ底部近傍の除染液流速を確保するために
当該部に気泡を発生させる口を設け、この気泡によって
除染液の流動を促進させることで請求項1の条件を達成
できる。A ninth aspect of the present invention is characterized in that a bubble generating port is provided at the bottom in the reactor pressure vessel or near the bottom of the jet pump to promote the flow of the decontamination liquid. According to the ninth aspect of the present invention, the decontamination liquid staying part in the reactor pressure vessel or the bottom part in the reactor pressure vessel that is a low flow rate part,
In order to secure the flow rate of the decontamination liquid near the bottom of the jet pump, a port for generating air bubbles is provided in the portion, and the flow of the decontamination liquid is promoted by the air bubbles, so that the condition of claim 1 can be achieved.
【0021】請求項10の発明は、原子炉圧力容器の底部
を貫通し林立して設けられた制御棒駆動機構案内管を取
り外し除染液の抜き出し口を形成して前記原子炉圧力容
器内底部の除染液の流動を促進することを特徴とする。According to a tenth aspect of the present invention, a control rod driving mechanism guide tube penetrating through the bottom of the reactor pressure vessel is removed to form a discharge port for a decontamination liquid, thereby forming a bottom of the reactor pressure vessel. Characterized by promoting the flow of the decontamination liquid.
【0022】請求項10の発明によれば、制御棒駆動機構
を取り外して除染液の取り出し口とし低流速部となって
いる原子炉圧力容器内底部の除染液流動性を向上させ請
求項1の条件を達成できる。According to the tenth aspect of the present invention, the control rod drive mechanism is removed to improve the flowability of the decontamination liquid at the bottom of the reactor pressure vessel, which is a low flow rate portion as a discharge port for the decontamination liquid. Condition 1 can be achieved.
【0023】請求項11の発明は、原子炉圧力容器のボト
ムドレンラインを使用して除染液の抜き出し口を形成し
て前記原子炉圧力容器内底部の除染液の流動を促進する
ことを特徴とする。[0023] The invention of claim 11 is that the bottom drain line of the reactor pressure vessel is used to form a discharge port for the decontamination solution to promote the flow of the decontamination solution inside the reactor pressure vessel. Features.
【0024】請求項11の発明によれば、原子炉圧力容器
のボトムラインから除染液を抜き出し、原子炉圧力容器
内底部の除染液の流動を促進させ、請求項1の条件を達
成できる。According to the eleventh aspect of the present invention, the decontamination liquid is extracted from the bottom line of the reactor pressure vessel, and the flow of the decontamination liquid at the bottom inside the reactor pressure vessel is promoted, so that the condition of the first aspect can be achieved. .
【0025】[0025]
【発明の実施の形態】図1および図2により本発明の請
求項1および2に対応する原子炉圧力容器内の除染方法
の第1および第2の実施の形態を説明する。図1は第1
の実施の形態に係る除染方法において除染に必要な最小
流動性(流速)の実験データを示している。すなわち、
たて軸は除染効率(DF)で、よこ軸は線流速(m/se
c )であり、図1の実験データから必要最小流速は1cm
/sec とすれば、除染効率が高まることが認められる。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First and second embodiments of a method for decontaminating a reactor pressure vessel according to claims 1 and 2 of the present invention will be described with reference to FIGS. Figure 1 shows the first
7 shows experimental data of minimum fluidity (flow rate) required for decontamination in the decontamination method according to the embodiment. That is,
The vertical axis is the decontamination efficiency (DF), and the horizontal axis is the linear flow velocity (m / se).
c), and the required minimum flow rate is 1 cm from the experimental data in FIG.
/ Sec, it is recognized that the decontamination efficiency increases.
【0026】この必要最小流速を達成するためには原子
炉再循環系の再循環ポンプ流量を定格の20%から30%で
運転することで、適正な流量、水位を確保することがで
きる。なお、除染液としては還元剤および酸化剤を使用
しするが、これらの除染液の成分は汚染物の種類、付着
状態によって取捨選択される。In order to achieve the required minimum flow velocity, an appropriate flow rate and water level can be secured by operating the reactor recirculation system at a recirculation pump flow rate of 20% to 30% of the rated value. Note that a reducing agent and an oxidizing agent are used as the decontamination liquid, and the components of these decontamination liquids are selected depending on the type of contaminant and the state of adhesion.
【0027】図2は第2の実施の形態を説明するための
図1の実験データを得る際に使用された原子炉圧力容器
と再循環系を示し、炉内化学除染を行う場合のフロー図
で、原子炉圧力容器1内からドライヤ,セパレータ,燃
料集合体,制御棒などは取り外された状態となってい
る。FIG. 2 shows a reactor pressure vessel and a recirculation system used for obtaining the experimental data of FIG. 1 for explaining the second embodiment, and a flow in the case of performing in-reactor chemical decontamination. In the figure, a dryer, a separator, a fuel assembly, a control rod, and the like have been removed from the reactor pressure vessel 1.
【0028】原子炉圧力容器1内の除染液の流動を得る
ために原子炉再循環系2を再循環ポンプ3によって循環
させ、原子炉圧力容器1内の底部、ジェットポンプ4の
底部近傍の除染液の流速を確保することができる。In order to obtain the flow of the decontamination liquid in the reactor pressure vessel 1, the reactor recirculation system 2 is circulated by the recirculation pump 3, and the bottom of the reactor pressure vessel 1 and the vicinity of the bottom of the jet pump 4 The flow rate of the decontamination liquid can be secured.
【0029】図2において、符号29はシュラウドで上部
格子板8と炉心支持板11を保持し、燃料集合体(図示せ
ず)全体を包んで炉心を形成するものである。炉心支持
板11は制御棒駆動機構5の制御棒案内管と燃料支持金具
を介して燃料集合体を保持する。ジェットポンプ4はシ
ュラウド29と原子炉圧力容器1との間に配置され、冷却
材を強制循環させる。In FIG. 2, reference numeral 29 denotes a shroud which holds the upper lattice plate 8 and the core support plate 11 and wraps the entire fuel assembly (not shown) to form a core. The core support plate 11 holds a fuel assembly via a control rod guide tube of the control rod drive mechanism 5 and a fuel support. The jet pump 4 is disposed between the shroud 29 and the reactor pressure vessel 1 to forcibly circulate the coolant.
【0030】原子炉再循環系2は原子炉圧力容器1の外
側に持続した再循環出口ノズル12,再循環配管6,2個
の再循環出入口弁14,再循環ポンプ3および再循環入口
ノズル13とからなっている。再循環ポンプ3は例えば竪
形単段斜流うず巻ポンプで、ポンプ軸は2段のメカニカ
ルシールでシールされ、軸封はポンプ軸に設けたポンプ
によって冷却水を流して冷却している。符号7は原子炉
圧力容器1内に冷却水を供給するための給水ノズル,9
は炉心スプレイライン,10は給水パージャを示してい
る。The reactor recirculation system 2 includes a recirculation outlet nozzle 12, a recirculation pipe 6, two recirculation inlet / outlet valves 14, a recirculation pump 3, and a recirculation inlet nozzle 13 which are maintained outside the reactor pressure vessel 1. It consists of The recirculation pump 3 is, for example, a vertical single-stage mixed flow spiral pump. The pump shaft is sealed with a two-stage mechanical seal, and the shaft seal is cooled by flowing cooling water by a pump provided on the pump shaft. Reference numeral 7 denotes a water supply nozzle for supplying cooling water into the reactor pressure vessel 1;
Denotes a core spray line, and 10 denotes a water supply purger.
【0031】本実施の形態によれば、原子炉圧力容器1
内の除染液の流動を得るために原子炉再循環系2を再循
環ポンプ3を運転して除染液を循環させ、原子炉圧力容
器1の底部およびジェットポンプ4の底部近傍の流速を
少なくとも1cm/秒に確保することができる。According to the present embodiment, the reactor pressure vessel 1
In order to obtain the flow of the decontamination liquid in the reactor, the decontamination liquid is circulated through the reactor recirculation system 2 by operating the recirculation pump 3, and the flow velocity near the bottom of the reactor pressure vessel 1 and the bottom of the jet pump 4 is reduced. At least 1 cm / sec can be secured.
【0032】以下、図3から図11により本発明の請求項
3から請求項11にそれぞれ対応する原子炉圧力容器内の
除染方法の第3から第11の実施の形態を説明する。な
お、図3から図11中で図2と同一部分には同一符号を付
して重複する部分の説明は省略し、各実施の形態におい
ては第2の実施の形態と異なる要点のみを説明する。Hereinafter, third to eleventh embodiments of the decontamination method in the reactor pressure vessel according to the third to eleventh aspects of the present invention will be described with reference to FIGS. 3 to 11, the same parts as those in FIG. 2 are denoted by the same reference numerals, and the description of the overlapping parts will be omitted. In each embodiment, only the points different from the second embodiment will be described. .
【0033】すなわち、第3の実施の形態が第2の実施
の形態と異なる点は図3に示すように原子炉圧力容器1
の底部に仮設水中ポンプ15を設置したことにある。この
仮設ポンプ15により局所的な流動をつくり除染効率を向
上させることができる。すなわち通常図3中Aで示す直
線的な流れになるところを仮設水中ポンプ15の駆動によ
り図3中Bで示すように噴水形の流れを形成することが
でき、第1の実施の形態の条件を達成することができ
る。That is, the third embodiment differs from the second embodiment in that the reactor pressure vessel 1 shown in FIG.
Is that a temporary submersible pump 15 is installed at the bottom of the. With this temporary pump 15, a local flow can be created and the decontamination efficiency can be improved. That is, a fountain-shaped flow can be formed as shown by B in FIG. 3 by driving the temporary submersible pump 15 where a linear flow usually shown by A in FIG. 3 is obtained. Can be achieved.
【0034】第4の実施の形態においては図4に示した
ように制御棒駆動機構5の案内管にCRD案内管キャッ
プ24を被せて原子炉圧力容器1内の底部の除染液の流動
を促進させたことにある。本実施の形態によれば、キャ
ップ24を被せることにより、案内管が閉塞されるので、
除染液が案内管内に流れ込むことがなく、原子炉圧力容
器1内の底部の除染液を所定の流速に維持することがで
きる。In the fourth embodiment, as shown in FIG. 4, the guide tube of the control rod driving mechanism 5 is covered with a CRD guide tube cap 24 to control the flow of the decontaminant at the bottom in the reactor pressure vessel 1. Has been promoted. According to the present embodiment, since the guide tube is closed by covering the cap 24,
The decontamination liquid does not flow into the guide tube, and the decontamination liquid at the bottom in the reactor pressure vessel 1 can be maintained at a predetermined flow rate.
【0035】第5の実施の形態においては図5に示した
ように原子炉圧力容器1内の底部およびジェットポンプ
4の底部にそれぞれ炉底部撹拌機18を吊りワイヤ30によ
り吊り下げて設けたことにある。この撹拌機18は仮設回
転体を設けることができ、この撹拌機18により原子炉圧
力容器1内の底部およびジェットポンプ4の底部の除染
液の撹拌を促進して所定の流速を確保できる。In the fifth embodiment, as shown in FIG. 5, a furnace bottom stirrer 18 is provided at the bottom of the reactor pressure vessel 1 and at the bottom of the jet pump 4 by being suspended by a suspension wire 30. It is in. The stirrer 18 can be provided with a temporary rotating body, and the stirrer 18 can promote the stirring of the decontamination liquid at the bottom of the reactor pressure vessel 1 and the bottom of the jet pump 4 to secure a predetermined flow rate.
【0036】第6の実施の形態においては図6に示した
ように原子炉圧力容器1内の中央部に仮設タンク21を設
置して原子炉圧力容器1内の底部の除染液の流動性を向
上させたことにある。この仮設タンク21の設置により除
染液量の低減を図ることができることと相俟って、原子
炉圧力容器1内底部の除染液の流動性の向上とともに均
一に除染効率が得られる流速をいきとどかせることが容
易となる。In the sixth embodiment, as shown in FIG. 6, a temporary tank 21 is provided at the center of the reactor pressure vessel 1 to make the fluidity of the decontamination liquid at the bottom of the reactor pressure vessel 1 lower. Has been improved. With the provision of the temporary tank 21, the amount of the decontamination liquid can be reduced, and the flow rate at which the decontamination liquid at the bottom of the reactor pressure vessel 1 is improved and the decontamination efficiency is obtained uniformly. It is easier to keep
【0037】第7の実施の形態においては図7に示した
ように原子炉圧力容器1内の底部およびジェットポンプ
4の近傍に機械洗浄機構として吸引洗浄装置26を設け、
この吸引洗浄装置26に仮設ポンプ27およびフィルタ28を
吸い込み配管31により接続し、かつフィルタ28の出口側
を戻り配管32により接続して、除染液を循環させること
によって除染効率を高めたことにある。In the seventh embodiment, as shown in FIG. 7, a suction cleaning device 26 is provided as a mechanical cleaning mechanism at the bottom of the reactor pressure vessel 1 and near the jet pump 4,
A temporary pump 27 and a filter 28 were connected to the suction cleaning device 26 by a suction pipe 31, and an outlet side of the filter 28 was connected by a return pipe 32, thereby increasing the decontamination efficiency by circulating the decontamination liquid. It is in.
【0038】本実施の形態によれば、原子炉圧力容器1
の底部や、ジェットポンプ4の底部近傍に1cm/秒の流
速が確保できない場合、化学除染後の吸引洗浄を行うも
ので、このような機械洗浄機構の併用によって除染効果
を高めることができる。機械洗浄機構としては吸引洗浄
のほかにジェット洗浄,散水洗浄,ブラシ洗浄,超音波
洗浄などを任意選択することができる。According to the present embodiment, the reactor pressure vessel 1
When a flow rate of 1 cm / sec cannot be secured at the bottom of the jet pump 4 or near the bottom of the jet pump 4, suction cleaning after chemical decontamination is performed, and the decontamination effect can be enhanced by using such a mechanical cleaning mechanism together. . As the mechanical cleaning mechanism, jet cleaning, sprinkling cleaning, brush cleaning, ultrasonic cleaning and the like can be arbitrarily selected in addition to suction cleaning.
【0039】第8の実施の形態においては図8に示した
ように原子炉圧力容器1内の底部およびジェットポンプ
4の底部の除染液の流動を促進するために、除染液出入
口16と除染液循環ライン17を設けたことにある。In the eighth embodiment, as shown in FIG. 8, in order to promote the flow of the decontamination liquid at the bottom of the reactor pressure vessel 1 and at the bottom of the jet pump 4, a decontamination liquid inlet / outlet 16 is provided. The decontamination liquid circulation line 17 is provided.
【0040】本実施の形態によれば、循環ライン17には
循環ポンプ33が接続されており、循環ポンプ33により除
染液は循環し所定の流速を得ることができる。すなわ
ち、流速の乏しい部位に除染液出入口16を設けることに
よって流れが形成されるためより効果的に除染を行うこ
とができる。According to the present embodiment, the circulation pump 17 is connected to the circulation line 17, and the decontamination liquid can be circulated by the circulation pump 33 to obtain a predetermined flow rate. That is, since the flow is formed by providing the decontamination liquid inlet / outlet 16 at a portion where the flow velocity is poor, decontamination can be performed more effectively.
【0041】第9の実施の形態においては図9に示した
ように第8の実施の形態に準じて原子炉圧力容器1内の
底部およびジェットポンプの底部に除染液の流動を促進
するために、気泡発生口19と気泡発生装置20および気泡
供給配管34を設けたことにある。本実施の形態によれば
気泡発生口19から気泡を除染液中に送り込むことにより
気泡による撹拌効果で除染液の流動を促進させることが
できる。In the ninth embodiment, as shown in FIG. 9, in order to promote the flow of the decontamination liquid to the bottom in the reactor pressure vessel 1 and the bottom of the jet pump according to the eighth embodiment. In addition, a bubble generating port 19, a bubble generating device 20, and a bubble supply pipe 34 are provided. According to the present embodiment, by sending bubbles into the decontamination liquid from the bubble generation port 19, the flow of the decontamination liquid can be promoted by the stirring effect of the bubbles.
【0042】第10の実施の形態においては図10に示した
ように原子炉圧力容器1内の制御棒駆動機構5を取り外
して除染液抜き出し口としてCRDからの仮設リングヘ
ッダ22を取り付け、この仮設リングヘッダ22に連結ライ
ン35の一端例を介して除染装置23を設けたことにある。
連結ライン35の他端側は原子炉圧力容器1内に開口して
いる。本実施の形態によれば除染液の抜き出し口を設け
ることにより原子炉圧力容器1内底部の除染液の流動を
促進できる。In the tenth embodiment, as shown in FIG. 10, the control rod drive mechanism 5 in the reactor pressure vessel 1 is removed, and a temporary ring header 22 from the CRD is attached as a decontamination liquid outlet. The decontamination device 23 is provided on the temporary ring header 22 via an example of one end of the connection line 35.
The other end of the connection line 35 opens into the reactor pressure vessel 1. According to the present embodiment, the flow of the decontamination liquid at the bottom of the reactor pressure vessel 1 can be promoted by providing the outlet for the decontamination liquid.
【0043】第11の実施の形態においては第10の実施の
形態に準じており、原子炉圧力容器1の底部にボトムラ
インとしてRPVドレンライン25を設けて除染液の抜き
出し口を形成して原子炉圧力容器1の底部の除染液の流
動を促進することにある。すなわち、原子炉圧力容器1
の底部を貫通するRPVドレンライン25を除染装置23を
備えた循環ラインを構成する連結ラインに接続する。The eleventh embodiment is similar to the tenth embodiment. An RPV drain line 25 is provided at the bottom of the reactor pressure vessel 1 as a bottom line to form a discharge port for a decontamination liquid. The purpose is to promote the flow of the decontamination liquid at the bottom of the reactor pressure vessel 1. That is, the reactor pressure vessel 1
The RPV drain line 25 penetrating through the bottom of is connected to a connection line constituting a circulation line provided with the decontamination device 23.
【0044】本実施の形態によれば、原子炉圧力容器1
内の除染液の流動を促進して底部の均一な流速を得るこ
とができ、その底部全体の除染効率の向上を高めること
ができる。According to the present embodiment, the reactor pressure vessel 1
By promoting the flow of the decontamination liquid in the inside, a uniform flow velocity at the bottom can be obtained, and the improvement of the decontamination efficiency of the entire bottom can be enhanced.
【0045】[0045]
【発明の効果】本発明によれば、原子炉圧力容器内の狹
溢部となっている原子炉圧力容器内底部やジェットポン
プの底部近傍に除染液を少なくとも1cm/秒の流速で流
して流動を与えることにより化学除染効果を向上させる
ことができる。According to the present invention, the decontamination liquid is caused to flow at a flow rate of at least 1 cm / sec to the bottom of the reactor pressure vessel or the vicinity of the bottom of the jet pump, which is a narrow overflow portion in the reactor pressure vessel. By imparting fluidity, the chemical decontamination effect can be improved.
【0046】また、除染液の液滞留部をなくす全ての除
染対象部位で必要な少なくとも1cm/秒の流速を得るた
めに、既設または仮設のポンプや循環ラインを使用した
り、これらの組み合わせによって除染液流量を所定の値
に制御することができ、十分な化学除染効果を得ること
ができる。Further, in order to obtain a necessary flow rate of at least 1 cm / sec at all the decontamination target sites for eliminating the liquid detained portion of the decontamination liquid, an existing or temporary pump or a circulation line may be used, or a combination thereof. As a result, the flow rate of the decontamination solution can be controlled to a predetermined value, and a sufficient chemical decontamination effect can be obtained.
【0047】さらに、十分な流速が得られない場合には
機械洗浄の併用により除染効果を高めることができ、こ
れにより如何なる原子炉圧力容器内補修作業も実施可能
となり、そのうえ大幅な放射線被曝の低減を図ることが
できる。Further, when a sufficient flow rate cannot be obtained, the decontamination effect can be enhanced by the combined use of mechanical cleaning, whereby any repair work in the reactor pressure vessel can be carried out, and furthermore, a large radiation exposure can be achieved. Reduction can be achieved.
【図1】本発明に係る原子炉圧力容器内の除染方法の第
1の実施の形態を説明するための実験データを示す曲線
図。FIG. 1 is a curve diagram showing experimental data for explaining a first embodiment of a decontamination method in a reactor pressure vessel according to the present invention.
【図2】本発明に係る原子炉圧力容器内の除染方法の第
2の実施の形態を示す概略断面図。FIG. 2 is a schematic sectional view showing a second embodiment of the decontamination method in the reactor pressure vessel according to the present invention.
【図3】本発明に係る原子炉圧力容器内の除染方法の第
3の実施の形態を示す概略断面図。FIG. 3 is a schematic sectional view showing a third embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図4】本発明に係る原子炉圧力容器内の除染方法の第
4の実施の形態を示す概略断面図。FIG. 4 is a schematic sectional view showing a fourth embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図5】本発明に係る原子炉圧力容器内の除染方法の第
5の実施の形態を示す概略断面図。FIG. 5 is a schematic sectional view showing a fifth embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図6】本発明に係る原子炉圧力容器内の除染方法の第
6の実施の形態を示す概略断面図。FIG. 6 is a schematic sectional view showing a sixth embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図7】本発明に係る原子炉圧力容器内の除染方法の第
7の実施の形態を示す概略断面図。FIG. 7 is a schematic sectional view showing a seventh embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図8】本発明に係る原子炉圧力容器内の除染方法の第
8の実施の形態を示す概略断面図。FIG. 8 is a schematic sectional view showing an eighth embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図9】本発明に係る原子炉圧力容器内の除染方法の第
9の実施の形態を示す概略断面図。FIG. 9 is a schematic sectional view showing a ninth embodiment of the method for decontaminating a reactor pressure vessel according to the present invention.
【図10】本発明に係る原子炉圧力容器内の除染方法の
第10の実施の形態を示す概略断面図。FIG. 10 is a schematic sectional view showing a decontamination method in a reactor pressure vessel according to a tenth embodiment of the present invention.
【図11】本発明に係る原子炉圧力容器内の除染方法の
第11の実施の形態を示す概略断面図。FIG. 11 is a schematic sectional view showing an eleventh embodiment of the decontamination method in the reactor pressure vessel according to the present invention.
1…原子炉圧力容器、2…原子炉再循環系、3…再循環
ポンプ、4…ジェットポンプ、5…制御棒駆動機構(C
RD)、6…再循環配管、7…給水ノズル、8…上部格
子板、9…炉心スプレイライン、10…給水スパージャ、
11…炉心支持板、12…再循環出口ノズル、13…再循環入
口ノズル、14…再循環出入口弁、15…仮設水中ポンプ、
16…除染液出入口、17…除染液循環ライン、18…炉底部
撹拌機、19…気泡発生口、20…気泡発生装置、21…仮設
タンク、22…CRDからの仮設リングヘッダ、23…除染
装置、24…CRD案内管キャップ、25…RPVドレンラ
イン、26…吸引洗浄装置、27…仮設ポンプ、28…フィル
タ、29…シュラウド、30…吊りワイヤ、31…吸込配管、
32…戻り配管、33…循環ポンプ、24…気泡供給配管、35
…連結ライン。DESCRIPTION OF SYMBOLS 1 ... Reactor pressure vessel, 2 ... Reactor recirculation system, 3 ... Recirculation pump, 4 ... Jet pump, 5 ... Control rod drive mechanism (C
RD), 6: Recirculation pipe, 7: Water supply nozzle, 8: Upper lattice plate, 9: Core spray line, 10: Water supply sparger,
11 core support plate, 12 recirculation outlet nozzle, 13 recirculation inlet nozzle, 14 recirculation inlet / outlet valve, 15 temporary water pump,
16 ... decontamination liquid inlet / outlet, 17 ... decontamination liquid circulation line, 18 ... furnace bottom stirrer, 19 ... bubble generation port, 20 ... bubble generation device, 21 ... temporary tank, 22 ... temporary ring header from CRD, 23 ... Decontamination device, 24 CRD guide tube cap, 25 RPV drain line, 26 Suction cleaning device, 27 Temporary pump, 28 Filter, 29 Shroud, 30 Hanging wire, 31 Suction pipe,
32… Return piping, 33… Circulation pump, 24… Bubble supply piping, 35
... connecting line.
Claims (11)
ドとの間に炉水を強制循環させるジェットポンプが設け
られ、このジェットポンプからの炉水を前記原子炉圧力
容器の下部外面に接続した再循環系入口ノズルおよび出
口ノズルを通して循環させる再循環系配管および再循環
ポンプが設けられ、この再循環ポンプの駆動により前記
原子炉圧力容器内に供給した除染液に流動を付与する原
子炉圧力容器内の化学除染方法において、前記原子炉圧
力容器内の底部または前記ジェットポンプの底部近傍に
流す除染液の流速を少なくとも1cm/秒に選定して前記
除染液に流動を付与することを特徴とする原子炉圧力容
器内の除染方法。1. A jet pump for forcibly circulating reactor water between a shroud installed in a reactor pressure vessel is provided, and reactor water from the jet pump is connected to a lower outer surface of the reactor pressure vessel. A recirculation pipe and a recirculation pump for circulating through a recirculation system inlet nozzle and an outlet nozzle are provided, and a reactor pressure for applying a flow to the decontamination liquid supplied into the reactor pressure vessel by driving the recirculation pump. In the method of chemical decontamination in a vessel, the flow rate of the decontamination liquid flowing at the bottom in the reactor pressure vessel or near the bottom of the jet pump is selected to be at least 1 cm / sec to impart a flow to the decontamination liquid. A decontamination method in a reactor pressure vessel, characterized by the following.
ら30%の回転数で運転して前記除染液に流動を付与する
ことを特徴とする請求項1記載の原子炉圧力容器内の除
染方法。2. The reactor pressure vessel according to claim 1, wherein the recirculation pump is operated at a rotation speed of 20% to 30% of a rated operation to impart a flow to the decontamination liquid. Decontamination method.
炉圧力容器内に設置されたジェットポンプの底部近傍に
仮設水中ポンプを吊り降ろして前記水中ポンプの駆動に
より前記除染液に流動を付与することを特徴とする請求
項1記載の原子炉圧力容器内の除染方法。3. A temporary submersible pump is suspended from the bottom of the reactor pressure vessel or near the bottom of a jet pump installed in the reactor pressure vessel, and the decontamination liquid is given a flow by driving the submersible pump. The method for decontamination in a reactor pressure vessel according to claim 1, wherein
する複数の制御棒駆動機構案内管の上端開口にキャップ
を被せて前記原子炉圧力容器底部の除染液の流れを分散
させて流動を促進させることを特徴とする請求項1記載
の原子炉圧力容器内の除染方法。4. A cap is placed on an upper end opening of a plurality of control rod drive mechanism guide tubes penetrating from the bottom inside the reactor pressure vessel to disperse and flow the decontamination liquid at the bottom of the reactor pressure vessel. The method for decontamination in a reactor pressure vessel according to claim 1, wherein the decontamination is promoted.
ットポンプの底部に回転体を設けて前記各底部の除染液
の撹拌を促進することを特徴とする請求項1記載の原子
炉圧力容器内の除染方法。5. The reactor pressure vessel according to claim 1, wherein a rotating body is provided at the bottom of the reactor pressure vessel or at the bottom of the jet pump to promote agitation of the decontamination liquid at each of the bottoms. Decontamination method inside.
ンクを設置して前記原子炉圧力容器底部の除染液の流動
性を向上させることを特徴とする請求項1記載の原子炉
圧力容器内の除染方法。6. The reactor according to claim 1, wherein a large-diameter temporary tank is provided at a central portion in the reactor pressure vessel to improve the flowability of the decontamination liquid at the bottom of the reactor pressure vessel. Decontamination method in pressure vessel.
を併用することを特徴とする請求項1記載の原子炉圧力
容器内の除染方法。7. The method for decontamination in a reactor pressure vessel according to claim 1, wherein a mechanical decontamination function in the reactor pressure vessel is used together.
ットポンプ底部に除染液の流動を促進する除染液の出口
または入口あるいはその両者を設けることを特徴とする
請求項1記載の原子炉圧力容器内の除染方法。8. The reactor according to claim 1, wherein a decontamination liquid outlet and / or an inlet for facilitating the flow of the decontamination liquid are provided at the bottom of the reactor pressure vessel or at the bottom of the jet pump. Decontamination method in pressure vessel.
ットポンプの底部近傍に気泡発生口を設けて除染液の流
動を促進することを特徴とする請求項1記載の原子炉圧
力容器内の除染方法。9. The reactor pressure vessel according to claim 1, wherein a bubble generating port is provided at the bottom of the reactor pressure vessel or near the bottom of the jet pump to promote the flow of the decontamination liquid. Decontamination method.
て設けられた制御棒駆動機構案内管を取り外し除染液の
抜き出し口を形成して前記原子炉圧力容器内底部の除染
液の流動を促進することを特徴とする請求項1記載の原
子炉圧力容器内の除染方法。10. A control rod drive mechanism guide tube which penetrates the bottom of the reactor pressure vessel and is provided in a standing state is formed to form a discharge port for the decontamination solution, and the decontamination solution at the bottom inside the reactor pressure vessel is formed. The method for decontamination in a reactor pressure vessel according to claim 1, wherein the flow is promoted.
を使用して除染液の抜き出し口を形成して前記原子炉圧
力容器内底部の除染液の流動を促進することを特徴とす
る請求項1記載の原子炉圧力容器内の除染方法。11. A decontamination liquid discharge port is formed by using a bottom drain line of a reactor pressure vessel to promote the flow of the decontamination liquid at the bottom inside the reactor pressure vessel. 2. The method for decontamination in a reactor pressure vessel according to claim 1.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16590497A JP3905955B2 (en) | 1997-06-23 | 1997-06-23 | Decontamination method for reactor pressure vessels |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16590497A JP3905955B2 (en) | 1997-06-23 | 1997-06-23 | Decontamination method for reactor pressure vessels |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH1114795A true JPH1114795A (en) | 1999-01-22 |
JP3905955B2 JP3905955B2 (en) | 2007-04-18 |
Family
ID=15821213
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16590497A Expired - Lifetime JP3905955B2 (en) | 1997-06-23 | 1997-06-23 | Decontamination method for reactor pressure vessels |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3905955B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004183923A (en) * | 2002-11-29 | 2004-07-02 | Sumitomo Titanium Corp | Method and device for flushing melting furnace |
-
1997
- 1997-06-23 JP JP16590497A patent/JP3905955B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004183923A (en) * | 2002-11-29 | 2004-07-02 | Sumitomo Titanium Corp | Method and device for flushing melting furnace |
Also Published As
Publication number | Publication date |
---|---|
JP3905955B2 (en) | 2007-04-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6270880B2 (en) | Chemical decontamination method | |
JP6226646B2 (en) | Reactor pressure vessel decontamination method and decontamination system thereof | |
US5124115A (en) | Bwr series pump recirculation system | |
JP2017223524A (en) | Chemical decontamination system and chemical decontamination method of reactor pressure vessel | |
JP6470467B1 (en) | Decontamination method | |
JP3160461B2 (en) | Recirculation system with jet pump and furnace pump | |
CN107408415A (en) | For the method to refrigerant injection gas and control system and nuclear reactor facility | |
JP3172127B2 (en) | Chemical decontamination method for facilities in nuclear power plants | |
KR920002562B1 (en) | Flow control method for radioactive decontamination of nuclear steam generator | |
JPH1114795A (en) | Decontaminating method for reactor pressure vessel | |
JP2007212293A (en) | Chemical decontaminating apparatus and decontaminating method of same | |
JP4183714B2 (en) | In-furnace chemical decontamination apparatus and decontamination method thereof | |
JP6467080B1 (en) | Decontamination method and decontamination device | |
JP6505810B1 (en) | Decontamination implementation method and decontamination implementation device | |
US6506955B1 (en) | Decontamination method | |
JP2005069898A (en) | Decontamination device for facility in nuclear power plant and its decontamination method | |
US5307389A (en) | System for removing liquid waste from a tank | |
JPH1114796A (en) | Decontamination method for inside nuclear reactor pressure vessel and decontamination device thereof | |
CN219297178U (en) | Cooling water dosing equipment | |
JPH02272398A (en) | Waste liquid storage device | |
JPS60256100A (en) | Method of decontaminating nuclear reactor system piping | |
JP7094900B2 (en) | Decontamination method and decontamination equipment | |
JPH09327618A (en) | Liquid stirring tank | |
JP2933334B2 (en) | Emergency core cooling system of boiling water nuclear power plant and its operation method. | |
JP2021096189A (en) | Decontamination implementation method and decontamination implementation apparatus |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20050309 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20050412 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20050613 |
|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20060816 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20061013 |
|
A911 | Transfer of reconsideration by examiner before appeal (zenchi) |
Free format text: JAPANESE INTERMEDIATE CODE: A911 Effective date: 20061025 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20061128 |
|
A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20061208 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20070109 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20070115 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20110119 Year of fee payment: 4 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20120119 Year of fee payment: 5 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130119 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20130119 Year of fee payment: 6 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20140119 Year of fee payment: 7 |
|
EXPY | Cancellation because of completion of term |