JP3010943B2 - Reduction chemical decontamination method for radioactive metal waste - Google Patents

Reduction chemical decontamination method for radioactive metal waste

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Publication number
JP3010943B2
JP3010943B2 JP4312784A JP31278492A JP3010943B2 JP 3010943 B2 JP3010943 B2 JP 3010943B2 JP 4312784 A JP4312784 A JP 4312784A JP 31278492 A JP31278492 A JP 31278492A JP 3010943 B2 JP3010943 B2 JP 3010943B2
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Japan
Prior art keywords
metal waste
decontamination
radioactive metal
radioactive
electrolytic reduction
Prior art date
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JP4312784A
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Japanese (ja)
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JPH06138295A (en
Inventor
明雄 田中
務 大沼
等 佐藤
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日立プラント建設株式会社
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、放射性金属廃棄物の化
学除染方法に係り、特に、金属廃棄物の汚染が廃棄物表
面に強固に付着したクラッド(汚染酸化皮膜)だけでな
く、金属母材内部にも浸透拡散しているステンレス鋼製
の放射性金属廃棄物の還元化学除染方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for chemical decontamination of radioactive metal waste, and more particularly to a method of chemically contaminating radioactive metal waste in addition to cladding (contaminated oxide film) in which metal waste is strongly adhered to the surface of waste. The present invention relates to a method for reducing chemical decontamination of stainless steel radioactive metal waste which has also penetrated and diffused into a base material.

【0002】[0002]

【従来の技術】原子力発電所などで発生する放射性金属
廃棄物は、主に配管、バルブ等の廃材であり、従来、こ
の種の廃棄物は細断するなどの方法でドラム缶等の専用
容器に入れ、廃棄物貯蔵庫に保管貯蔵されている。しか
し、その数は、年々累積し、その保管場所の確保が大き
な問題となっている。そのため、この種の金属廃棄物の
減容化が求められ、圧縮や加熱溶融により減容する方法
が提案されている。しかしながら、これらの方法では放
射性物質で汚染されている表面の汚染部分と大部分の非
汚染部分とを一括処理するため、その減容効果は顕著と
は言いがたい。
2. Description of the Related Art Radioactive metal waste generated in nuclear power plants is mainly waste materials such as pipes and valves. Conventionally, this kind of waste is cut into dedicated containers such as drums by shredding. And stored in waste storage. However, the number is accumulated year by year, and securing a storage place is a major problem. Therefore, it is required to reduce the volume of this type of metal waste, and a method of reducing the volume by compression or heating and melting has been proposed. However, in these methods, since the contaminated portion of the surface contaminated with the radioactive substance and most of the non-contaminated portion are treated collectively, the volume reduction effect cannot be said to be remarkable.

【0003】一方、表面の汚染部分のみを除去し、大半
の非汚染部分を一般廃棄物と同様に処分することを可能
とする除染・減容処理が放射性金属廃棄物の減容技術と
して有望視されている。この除染・減容化技術として
は、電解除染法、ブラスト除染法などが開発されている
が、これらの方法では除染対象物に電極あるいはノズル
を挿入する必要があり、バルブ、ポンプ等の複雑な形状
物の除染が難しいとされている。このような複雑な形状
物に適用できる除染法としては、除染液中に金属廃棄物
を浸漬し、汚染表面を溶解する化学除染法が最も一般的
である。除染液としては、シュウ酸、クエン酸のような
有機酸を主体としたもの、硫酸、硝酸、塩酸、フッ酸の
ような強酸が用いられるが、迅速かつ確実に除染を達成
する必要のある除染減容の目的には、金属に対する溶解
能力の大きな強酸が用いられる。
On the other hand, a decontamination / volume reduction process that removes only the contaminated portion of the surface and allows most non-polluted portions to be disposed of in the same manner as general waste is promising as a technology for reducing the volume of radioactive metal waste. Have been watched. Electrode-release and blast decontamination methods have been developed as decontamination and volume reduction technologies.However, these methods require the insertion of electrodes or nozzles into the object to be decontaminated, and require valves and pumps. It is said that it is difficult to decontaminate complicated shapes such as. The most common decontamination method applicable to such complicated shapes is a chemical decontamination method in which metal waste is immersed in a decontamination solution to dissolve the contaminated surface. As the decontamination liquid, those mainly composed of organic acids such as oxalic acid and citric acid, and strong acids such as sulfuric acid, nitric acid, hydrochloric acid and hydrofluoric acid are used, but it is necessary to quickly and surely achieve decontamination. For the purpose of certain decontamination volume reduction, a strong acid having a large dissolving capacity for metals is used.

【0004】ところで、放射性汚染がクラッドだけでな
く、金属母材中にも存在する放射性金属廃棄物を一般廃
棄物並みの放射能レベルまで除染するには、クラッド及
び金属母材の両者を効率よく溶解除去しうる化学除染法
が必要となる。一般に、ステンレス鋼製の金属廃棄物に
は、緻密な不働態皮膜が存在するため、硫酸等の強酸溶
液中に単に浸漬しただけでは酸溶解はほとんど進行しな
い。このため、硝酸又は硫酸に4価のセリウム等の酸化
剤を添加した溶液を用いてステンレス鋼製の金属母材を
酸化溶解し、クラッドを剥離除去する除染方法が提案さ
れている(例えば、特開昭61−204597号公
報)。しかし、この方法では、高価な4価のセリウムが
多量に消費されるため、電解操作によりセリウムを再生
する必要があり、装置や操作が複雑化するという問題が
あった。
By the way, in order to decontaminate radioactive metal waste not only in the clad but also in the metal base material to a radioactivity level equivalent to that of general waste, both the clad and the metal base material need to be efficiently treated. A chemical decontamination method that can be dissolved and removed well is required. In general, since a dense passive film is present in stainless steel metal waste, acid dissolution hardly progresses simply by dipping in a strong acid solution such as sulfuric acid. Therefore, a decontamination method has been proposed in which a metal base material made of stainless steel is oxidized and dissolved using a solution in which an oxidizing agent such as tetravalent cerium or the like is added to nitric acid or sulfuric acid, and the clad is peeled off (for example, JP-A-61-204597). However, this method consumes a large amount of expensive tetravalent cerium, so that it is necessary to regenerate cerium by an electrolytic operation, and there has been a problem that the apparatus and operation are complicated.

【0005】そのため、ステンレス鋼製の放射性金属廃
棄物の表面のクラッドや緻密な不働態皮膜を破壊し、溶
解するため、外部電源を用いて電気化学的に還元溶解し
た後、酸化剤を添加した硫酸溶液中で金属母材の酸溶解
を行うことにより、4価のセリウム等の酸化剤の使用量
を節減する方法が提案されている(特開平2−2259
7号公報)。しかし、この方法においては第一工程とし
て電解還元を行うため大面積を有する除染対象物に対し
ては、電解還元に要する電圧・電流が大きくなり、大容
量の直流電源が必要となり、また、これに伴って電源ケ
ーブルが太くなるなど、装置が複雑化するという問題が
あった。
[0005] Therefore, in order to break and dissolve the cladding and the dense passive film on the surface of the radioactive metal waste made of stainless steel, it is electrochemically reduced and dissolved using an external power supply, and then an oxidizing agent is added. A method has been proposed in which the amount of an oxidizing agent such as tetravalent cerium is reduced by dissolving a metal base material in acid in a sulfuric acid solution (JP-A-2-2259).
No. 7). However, in this method, for the decontamination target having a large area to perform electrolytic reduction as the first step, the voltage and current required for electrolytic reduction become large, and a large-capacity DC power supply is required. Along with this, there has been a problem that the apparatus becomes complicated, for example, the power cable becomes thicker.

【0006】[0006]

【発明が解決しようとする課題】本発明は、前記従来技
術の欠点を解消し、大面積を有するステンレス鋼製の放
射性金属廃棄物でも効率よく除染でき、電解還元に要す
る直流電源を小型化することができ、しかも酸化剤を添
加する必要のない化学除染方法を提供することを目的と
する。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned drawbacks of the prior art and can efficiently decontaminate radioactive metal waste made of stainless steel having a large area, and reduces the size of the DC power supply required for electrolytic reduction. It is an object of the present invention to provide a chemical decontamination method which can be carried out without adding an oxidizing agent.

【0007】[0007]

【課題を解決するための手段】本発明は、ステンレス鋼
の強酸溶液中での溶解特性を利用し、すなわち、電解還
元によりステンレス鋼の一部分を一時的に活性溶解域に
保持すると、クラッドや不働態皮膜が破壊され、溶解反
応が始まり、電解還元操作を停止した後も、局部電池の
作用により次々と溶解反応がステンレス鋼全体に伝播
し、強酸溶液中でクラッドや不働態皮膜が化学的に溶解
除去されることを利用し、金属廃棄物の一部分を強酸除
染液と接触させて電解還元を行った後に、全体を除染液
と接触させて除染液中で化学除染を行うことによって、
上記課題を達成したものである。
The present invention utilizes the dissolution characteristics of stainless steel in a strong acid solution. That is, when a portion of stainless steel is temporarily held in an active dissolution zone by electrolytic reduction, cladding or non-cladding occurs. The active film is destroyed, the dissolution reaction starts, and even after the electrolytic reduction operation is stopped, the dissolution reaction propagates to the entire stainless steel one after another by the action of the local battery, and the cladding and passive film are chemically formed in a strong acid solution. Performing electrolytic reduction by contacting a part of metal waste with strong acid decontamination solution using the fact that it is dissolved and removed, and then performing chemical decontamination in the decontamination solution by contacting the whole with the decontamination solution By
The above object has been achieved.

【0008】すなわち、本発明による放射性金属廃棄物
の還元化学除染方法は、放射性金属廃棄物を強酸除染液
に浸漬した初期に、所定時間電解還元した後、該金属廃
棄物表面を強酸除染液に化学溶解させて放射性物質を除
去することにより放射性金属廃棄物を除染する方法にお
いて、前記電解還元操作を、該金属廃棄物の一部分を強
酸除染液と接触させ、その部分に電圧電流を印加し、金
属廃棄物の浸漬電位を活性溶解域になるように所定時間
保持することによって行い、その後電解還元操作を停止
し、次いで該金属廃棄物全体を前記除染液に浸漬し、化
学溶解させて除染することを特徴とする。
That is, according to the method for reducing chemical decontamination of radioactive metal waste according to the present invention, the radioactive metal waste is electrolytically reduced for a predetermined time at the initial stage of immersion in a strong acid decontamination solution, and then the surface of the metal waste is subjected to strong acid decontamination. In a method of decontaminating radioactive metal waste by removing a radioactive substance by chemically dissolving in a dyeing liquor, the electrolytic reduction operation is performed by contacting a part of the metal waste with a strong acid decontamination liquid and applying a voltage to the part. An electric current is applied, and the immersion potential of the metal waste is maintained for a predetermined time so as to be in the active dissolving region.After that, the electrolytic reduction operation is stopped, and then the entire metal waste is immersed in the decontamination solution, It is characterized by chemical dissolution and decontamination.

【0009】本発明の方法において、放射性金属廃棄物
の一部分だけを除染液と接触させる方法としては、放射
性金属廃棄物を導電性の吊り具で吊り下げ、下部の一部
分のみを除染液に浸漬するか、又は金属廃棄物の表面の
一部分を露出させ、残りの部分を着脱可能な非導電性遮
蔽体で覆った放射性金属廃棄物の全体を除染液中に浸漬
することによって行うことができる。このようにして、
金属廃棄物表面の一部分だけを除染液と接触させて電解
還元操作を行い、電解還元操作を停止した後、後者の方
法の場合には前記非導電性遮蔽体を取り除いた後、金属
廃棄物全体を前記除染液に浸漬することによって、化学
溶解を進行させる。
In the method of the present invention, as a method of bringing only a part of the radioactive metal waste into contact with the decontamination liquid, the radioactive metal waste is hung by a conductive hanging tool, and only a part of the lower part is converted into the decontamination liquid. This can be done by immersing or immersing the entire radioactive metal waste in a decontamination liquid, exposing a part of the surface of the metal waste and covering the remaining part with a removable non-conductive shield. it can. In this way,
Performing an electrolytic reduction operation by bringing only a part of the surface of the metal waste into contact with the decontamination liquid, stopping the electrolytic reduction operation, and removing the non-conductive shield in the case of the latter method, and then removing the metal waste. By immersing the whole in the decontamination solution, chemical dissolution proceeds.

【0010】本発明の方法では、除染液としては、硫
酸、硝酸等の強酸を用いるが、以下には説明を簡明にす
るため、硫酸を用いた場合について説明する。ステンレ
ス鋼製母材の硫酸除染液(H2 SO4 濃度1.8モル/
l、温度80℃)中での溶解特性を示す分極(電位−電
流)曲線を図3に示す。図3において、不働態域にある
ステンレス鋼製の放射性金属廃棄物を硫酸除染液中に浸
漬し、電位を卑な方向に操作し、具体的には金属廃棄物
を陰極とし、ステンレス鋼が化学的に溶解する活性態域
に入るように一定時間電位を操作する。この電位を達成
するのに必要な電流は、金属廃棄物の除染面積に比例し
て大きくなる。具体的には、1m2 の汚染面に対しては
約100Aの直流電源を必要とした。ところで、本発明
における化学反応は、(1)式のように進行し、金属廃
棄物表面のクラッドや不働態皮膜は、還元溶解により破
壊され、金属母材が露出する。 MO+2H+ +e→M+ +H2 O ・・・(1)
In the method of the present invention, a strong acid such as sulfuric acid or nitric acid is used as a decontamination solution. Hereinafter, the case where sulfuric acid is used will be described for simplicity. Sulfuric acid decontamination solution for stainless steel base material (H 2 SO 4 concentration 1.8 mol /
FIG. 3 shows a polarization (potential-current) curve showing the dissolution characteristics in (I, temperature 80 ° C.). In FIG. 3, the stainless steel radioactive metal waste in the passive region is immersed in a sulfuric acid decontamination solution, and the electric potential is operated in a negative direction. The potential is manipulated for a period of time to enter the chemically active active region. The current required to achieve this potential increases in proportion to the area of decontamination of the metal waste. Specifically, a DC power supply of about 100 A was required for a 1 m 2 contaminated surface. By the way, the chemical reaction in the present invention proceeds as shown in equation (1), and the cladding and the passive film on the surface of the metal waste are destroyed by reduction and dissolution, exposing the metal base material. MO + 2H + + e → M + + H 2 O (1)

【0011】これにより露出し、活性化された金属母材
は、(2)式に示すように溶解を開始し、この時に電子
を放出する。 M→M+ +e ・・・(2) この電子によって、残存しているクラッドや不働態皮膜
は、電解還元なしに下記の(3)式に示すように還元溶
解される。 MO+2H+ +e→M+ +H2 O ・・・(3) すなわち、(1)式の反応が金属廃棄物の一部分で起こ
れば、(2)及び(3)式の反応は次々に進行すること
となるので、金属廃棄物全体に電圧・電流を印加する必
要はないこととなる。そこで、電解還元操作を停止した
後、金属廃棄物全体を除染液中に浸漬させ、上記反応を
進行させる。
The exposed and activated metal base material starts melting as shown in the equation (2), and emits electrons at this time. M → M + + e (2) The remaining cladding and passive film are reduced and dissolved by the electrons without electrolytic reduction as shown in the following equation (3). MO + 2H + + e → M + + H 2 O (3) That is, if the reaction of the formula (1) occurs in a part of the metal waste, the reactions of the formulas (2) and (3) proceed one after another. Therefore, it is not necessary to apply voltage and current to the entire metal waste. Therefore, after stopping the electrolytic reduction operation, the entire metal waste is immersed in a decontamination solution to allow the above reaction to proceed.

【0012】[0012]

【実施例】次に、図面を参照して本発明の実施例を詳細
に説明する。図1は本発明の一実施例を示す説明図であ
る。図1において、放射性金属廃棄物1の下部の一部だ
けを除染槽2中の除染液3中に浸漬し、直流電源4の陰
極側に接続し、陽極に接続した電極5との間で電解を行
う。このときの電位は、白金電極等の参照電極7と電位
測定装置6によって計測される。放射性金属廃棄物1の
一部分を上記の電解還元装置によって活性溶解域に若干
時間(具体的には5分間程度)保持することにより、表
面のクラッドや不働態酸化皮膜は溶解除去され、金属母
材の溶解反応が始まる。この後、放射性金属廃棄物1全
体を除染槽2中の除染液3中に浸漬することにより、前
記(1)〜(3)式の反応によって全体の溶解反応が進
行し、除染が達成される。
Next, an embodiment of the present invention will be described in detail with reference to the drawings. FIG. 1 is an explanatory diagram showing one embodiment of the present invention. In FIG. 1, only a part of the lower part of the radioactive metal waste 1 is immersed in a decontamination solution 3 in a decontamination tank 2, connected to the cathode side of the DC power supply 4, and between the electrode 5 connected to the anode. To perform electrolysis. The potential at this time is measured by a reference electrode 7 such as a platinum electrode and the potential measuring device 6. By holding a part of the radioactive metal waste 1 in the active dissolution zone for a short period of time (specifically, about 5 minutes) by the above-described electrolytic reduction apparatus, the cladding and passive oxide film on the surface are dissolved and removed, and the metal base material is removed. The dissolution reaction starts. Thereafter, the entire radioactive metal waste 1 is immersed in the decontamination solution 3 in the decontamination tank 2, whereby the entire dissolution reaction proceeds by the reactions of the above formulas (1) to (3), and decontamination is performed. Achieved.

【0013】図2は、本発明の他の実施例を示す説明図
である。図2に示した方法では、放射性金属廃棄物1の
一部分だけを露出し、残りの部分を着脱可能で、かつ非
導電性の遮蔽体8で覆うことにより、露出した一部分だ
けを除染液3と接触させて、前記と同様に電解還元操作
を行い、電解還元操作を停止した後、遮蔽体8を取り除
き、放射性金属廃棄物1全体を除染液3と接触させて溶
解反応を進行させ、除染を達成する。この方法に用いる
遮蔽体8の素材としては、プラスチック等の非導電性材
料が挙げられる。
FIG. 2 is an explanatory view showing another embodiment of the present invention. In the method shown in FIG. 2, only a part of the radioactive metal waste 1 is exposed, and the remaining part is covered with a detachable and non-conductive shield 8, so that only the exposed part is decontaminated liquid 3 , The electrolytic reduction operation is performed in the same manner as described above, and after the electrolytic reduction operation is stopped, the shield 8 is removed, and the entire radioactive metal waste 1 is brought into contact with the decontamination solution 3 to allow the dissolution reaction to proceed. Achieve decontamination. As a material of the shield 8 used in this method, a non-conductive material such as plastic is used.

【0014】次に、実際の除染実験により本発明の効果
を具体的に数値をもって説明する。従来法では1m2
面積を有する金属廃棄物では100Aの電流を必要と
し、これにさらに通電治具等への電流を加えると、12
0Aの電源容量を持つ電源設備を必要とした。一方、本
発明によれば、約1/5の面積への通電で充分であり、
通電治具への余分な電流も必要がないことから、20A
で除染を達成することができた。さらに、除染に要する
浸漬溶解時間もほとんど変わることがなかった。この実
験結果を表1に示す。
Next, the effects of the present invention will be concretely described by numerical values through actual decontamination experiments. In the conventional method, a metal waste having an area of 1 m 2 requires a current of 100 A, and when a current to a current-carrying jig or the like is further applied, a current of 12 A is obtained.
Power supply equipment having a power supply capacity of 0 A was required. On the other hand, according to the present invention, it is sufficient to energize about 1/5 of the area,
Since there is no need for extra current to the current-carrying jig, 20 A
Decontamination could be achieved. Furthermore, the immersion dissolution time required for decontamination hardly changed. Table 1 shows the experimental results.

【0015】[0015]

【表1】 [Table 1]

【0016】[0016]

【発明の効果】本発明の方法によれば、活性溶解域での
反応を起こさせるのに必要な、電解還元操作での直流電
源容量を少なくすることができ、大面積を有するステン
レス鋼製の放射性金属廃棄物を除染する場合でも、除染
設備の小型化、簡素化及び必要電気量の省力化が可能と
なる。また、高価な酸化剤を添加することなく化学溶解
を行うことができる。
According to the method of the present invention, it is possible to reduce the DC power supply capacity required for causing a reaction in the active dissolution zone in the electrolytic reduction operation, and it is possible to reduce the capacity of stainless steel having a large area. Even in the case of decontaminating radioactive metal waste, it is possible to reduce the size and simplification of decontamination equipment and to reduce the required amount of electricity. Further, chemical dissolution can be performed without adding an expensive oxidizing agent.

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

【図1】本発明の一実施例を示す説明図である。FIG. 1 is an explanatory diagram showing one embodiment of the present invention.

【図2】本発明の他の実施例を示す説明図である。FIG. 2 is an explanatory view showing another embodiment of the present invention.

【図3】硫酸除染液中でのステンレス鋼の分極曲線図で
ある。
FIG. 3 is a polarization curve diagram of stainless steel in a sulfuric acid decontamination solution.

【符号の説明】[Explanation of symbols]

1 放射性金属廃棄物 2 除染槽 3 除染液 4 直流電源 5 電極 6 電位測定装置 7 参照電極 8 遮蔽体 Reference Signs List 1 radioactive metal waste 2 decontamination tank 3 decontamination liquid 4 DC power supply 5 electrode 6 potential measurement device 7 reference electrode 8 shield

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) G21F 9/28 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) G21F 9/28

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 放射性金属廃棄物を強酸除染液に浸漬し
た初期に、所定時間電解還元した後、該金属廃棄物表面
を強酸除染液に化学溶解させて放射性物質を除去するこ
とにより放射性金属廃棄物を除染する方法において、前
記電解還元操作を、該金属廃棄物の一部分を強酸除染液
と接触させ、その部分に電圧電流を印加し、金属廃棄物
の浸漬電位を活性溶解域になるように所定時間保持する
ことによって行い、その後電解還元操作を停止し、次い
で該金属廃棄物全体を前記除染液に浸漬し、化学溶解さ
せて除染することを特徴とする放射性金属廃棄物の還元
化学除染方法。
At the initial stage of immersing a radioactive metal waste in a strong acid decontamination liquid, electrolytic reduction is performed for a predetermined time, and then the surface of the metal waste is chemically dissolved in the strong acid decontamination liquid to remove radioactive substances. In the method for decontaminating metal waste, the electrolytic reduction operation is performed by bringing a part of the metal waste into contact with a strong acid decontamination solution, applying a voltage / current to the part, and changing the immersion potential of the metal waste to an active dissolution zone. Radioactive metal waste, characterized in that the electrolytic reduction operation is stopped, and then the entire metal waste is immersed in the decontamination solution and chemically dissolved for decontamination. Method of reducing chemical decontamination of materials.
【請求項2】 放射性金属廃棄物を導電性の吊り具で吊
り下げ、下部の一部分のみを除染液に浸漬することによ
って金属廃棄物の一部分を除染液と接触させる請求項1
記載の放射性金属廃棄物の還元化学除染方法。
2. The method according to claim 1, wherein the radioactive metal waste is suspended by a conductive suspending tool, and only a part of the lower part is immersed in the decontamination liquid to bring a part of the metal waste into contact with the decontamination liquid.
The method for reduction chemical decontamination of radioactive metal waste according to the above.
【請求項3】 表面の一部分を露出させ、残りの部分を
着脱可能な非導電性遮蔽体で覆った放射性金属廃棄物の
全体を除染液中に浸漬することにより金属廃棄物の一部
分を除染液と接触させて電解還元操作を行い、電解還元
操作を停止した後、前記非導電性遮蔽体を取り除き、金
属廃棄物全体を前記除染液に浸漬する請求項1記載の放
射性金属廃棄物の還元化学除染方法。
3. A part of the metal waste is removed by immersing the whole of the radioactive metal waste in a decontamination solution, exposing a part of the surface and covering the remaining part with a removable non-conductive shield. The radioactive metal waste according to claim 1, wherein the non-conductive shield is removed and the entire metal waste is immersed in the decontamination solution after performing the electrolytic reduction operation by contacting with the dyeing solution and stopping the electrolytic reduction operation. Reduction chemical decontamination method.
JP4312784A 1992-10-28 1992-10-28 Reduction chemical decontamination method for radioactive metal waste Expired - Lifetime JP3010943B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4312784A JP3010943B2 (en) 1992-10-28 1992-10-28 Reduction chemical decontamination method for radioactive metal waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4312784A JP3010943B2 (en) 1992-10-28 1992-10-28 Reduction chemical decontamination method for radioactive metal waste

Publications (2)

Publication Number Publication Date
JPH06138295A JPH06138295A (en) 1994-05-20
JP3010943B2 true JP3010943B2 (en) 2000-02-21

Family

ID=18033365

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4312784A Expired - Lifetime JP3010943B2 (en) 1992-10-28 1992-10-28 Reduction chemical decontamination method for radioactive metal waste

Country Status (1)

Country Link
JP (1) JP3010943B2 (en)

Also Published As

Publication number Publication date
JPH06138295A (en) 1994-05-20

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