JPH0450699A - Method and apparatus for decontaminating radioactive solid contaminant - Google Patents

Method and apparatus for decontaminating radioactive solid contaminant

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Publication number
JPH0450699A
JPH0450699A JP15299090A JP15299090A JPH0450699A JP H0450699 A JPH0450699 A JP H0450699A JP 15299090 A JP15299090 A JP 15299090A JP 15299090 A JP15299090 A JP 15299090A JP H0450699 A JPH0450699 A JP H0450699A
Authority
JP
Japan
Prior art keywords
waste
cleaning agent
decontamination
tank
volume
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.)
Pending
Application number
JP15299090A
Other languages
Japanese (ja)
Inventor
Noriko Sagawa
佐川 紀子
Yoshikazu Kondou
賀計 近藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hitachi Ltd
Original Assignee
Hitachi Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP15299090A priority Critical patent/JPH0450699A/en
Publication of JPH0450699A publication Critical patent/JPH0450699A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To reduce the generation amount of waste by carrying out washing using a strong alkaline quaternary ammonium compound and thermally decomposing the waste washing solution after washing to reduce the volume thereof. CONSTITUTION:First, contaminant 2 is received in a decontaminating tank 3 and, next, a valve 9 is opened to send tetramethylammonium hydroxide in the decontaminating tank 3 from a detergent tank 1 and the contaminant 2 is immersed in a detergent for several min while stirred by a stirrer 7. After decontamination, valve 10 is opened to send out the waste detergent to a waste detergent tank 4 and the waste detergent tank 4 is heated from the circumfer ence in an electric furnace 5 to reduce the volume of the waste detergent under heating. The waste solution reduced in volume by heating is converted to solid waste, for example, by vitrification to be kept in predetermined place as radio active waste.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は放射性固体汚染物質の除染方法及びシステムに
係わり、特に、原子力施設から発生した放射性固体汚染
物質の除染において、洗浄後の廃棄物発生量の低減に好
適な除染方法及びシステムに関する。
[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a method and system for decontaminating radioactive solid contaminants, and in particular, in the decontamination of radioactive solid contaminants generated from nuclear facilities, the present invention relates to a method and system for decontaminating radioactive solid contaminants generated from nuclear facilities. The present invention relates to a decontamination method and system suitable for reducing the amount of waste generated.

〔従来の技術〕[Conventional technology]

従来の原子力施設における放射性固体汚染物質の除染に
は、化学的除染法、機械(物理)的除染法並びに電気・
磁気的除染法等の手法が用いられてきた。
Conventional decontamination of radioactive solid contaminants at nuclear facilities includes chemical decontamination methods, mechanical (physical) decontamination methods, and electrical/
Techniques such as magnetic decontamination have been used.

これら除染方法の中で化学的除染法は、例えば原子炉の
一次系などのような、強固な汚染物質を含む複雑なシス
テムを系統除染するのに適しており、各国で各種除染技
術の開発が行なわれている。
Among these decontamination methods, chemical decontamination methods are suitable for system decontamination of complex systems containing strong contaminants, such as the primary system of a nuclear reactor, and various decontamination methods are used in various countries. Technology is being developed.

この化学的除染法において、例えば金属表面の汚染物質
の除染方法の1つとして、酸、アルカリ、酸化剤、還元
剤等を単独或いは複数組合せて使用する方法が考えられ
ている。例えば、従来から行われている放射性固体汚染
物質の化学的除染法の1つとして、硝酸、純水、水酸化
ナトリウム並びにクエン酸、過酸化水素、酒石酸を組み
合わせた例が報告されている。例えば「原子力施設にお
ける除染技術」 (石搏顕吉慣習、NIC刊)、昭和5
9年版、第440頁には、トーンレイ(Doun+ca
y)再処理工場の放射性セルの除染において、高濃度硝
酸HNO,と高濃度水酸化ナトリウムNaOHの繰り返
し処理による方法を用い、65〜500R/hあった線
量が0.1〜1.2R/hに低下することが報告されて
いる。
In this chemical decontamination method, for example, a method of using an acid, an alkali, an oxidizing agent, a reducing agent, etc. singly or in combination is considered as one method for decontaminating contaminants on a metal surface. For example, as one of the conventional chemical decontamination methods for radioactive solid contaminants, a combination of nitric acid, pure water, sodium hydroxide, citric acid, hydrogen peroxide, and tartaric acid has been reported. For example, "Decontamination Techniques for Nuclear Facilities" (Kenkichi Ishiba's practice, published by NIC), 1932.
9th edition, page 440, Tonray (Doun+ca
y) In the decontamination of radioactive cells at a reprocessing plant, a method involving repeated treatment with high concentration nitric acid, HNO, and high concentration sodium hydroxide, NaOH, was used to reduce the dose from 65 to 500 R/h to 0.1 to 1.2 R/h. It has been reported that the temperature decreases to h.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

ところで、上記従来の除染方法では、除染試薬として水
酸化ナトリウムNaOH等の金属成分を含む化学物質を
用いているので、この金属成分と各種の試薬が反応して
、硝酸ナトリウムNaN0H3等の無機塩を生成し、除
染後に発生する廃洗浄剤中にはこの無機塩が含まれる。
By the way, in the conventional decontamination method described above, a chemical substance containing a metal component such as sodium hydroxide NaOH is used as a decontamination reagent, so this metal component and various reagents react to form inorganic substances such as sodium nitrate NaN0H3. This inorganic salt is contained in the waste cleaning agent generated after decontamination.

−船釣に化学的除染法では、除染後の廃院浄剤を蒸発濃
縮して減容処理する。このため、上記従来の除染方法で
は、廃院浄剤をある程度まで減容すると無機塩が沈澱す
る。このように無機塩が沈澱I、た場合には、生成した
塩を処理する濾過工程、脱水工程等の後続プロセスが必
要となる。従って、上記従来の除染方法では、無機塩が
沈澱i5ない程度に廃院浄剤の濃縮を止どめており、こ
のため廃院浄剤の減容が十分に行えず、大量の廃棄物が
発生するという問題があった。
- In the chemical decontamination method for boat fishing, the hospital cleaning agent after decontamination is evaporated and concentrated to reduce its volume. Therefore, in the conventional decontamination method described above, when the volume of the hospital cleaning agent is reduced to a certain extent, inorganic salts precipitate. When inorganic salts are precipitated in this manner, subsequent processes such as a filtration step and a dehydration step are required to treat the formed salts. Therefore, in the conventional decontamination method described above, the concentration of the waste hospital cleaning agent is stopped to the extent that inorganic salts do not precipitate. Therefore, the volume of the waste hospital cleaning agent cannot be reduced sufficiently, and a large amount of waste is generated. There was a problem that occurred.

本発明の目的は、廃棄物発生量を低減できる放射線固体
汚染物質の除染方法及びシステムを提供することである
An object of the present invention is to provide a method and system for decontaminating radioactive solid contaminants that can reduce the amount of waste generated.

〔課題を解決するための手段〕[Means to solve the problem]

本発明によれば、上記目的を達成するため、放射性固体
汚染物質の付着した固体金属表面の洗浄剤として強アル
カリ性の第4級アンモニウム化合物を用いて洗浄し、洗
浄後の廃院浄剤を加熱分解して減容することを特徴とす
る放射性固体汚染物質の除染方法が提供される。
According to the present invention, in order to achieve the above object, a strong alkaline quaternary ammonium compound is used as a cleaning agent to clean the solid metal surface to which radioactive solid contaminants have adhered, and the cleaning agent after cleaning is heated. A method for decontaminating radioactive solid contaminants is provided, which is characterized by decontaminating and reducing the volume of radioactive solid contaminants.

洗浄剤としてしよう可能な強アルカリ性の第4級アンモ
ニウム化合物の例としては、水酸化テトラメチルアンモ
ニウム、水酸化テトラエチルアンモニウム等がある。
Examples of strongly alkaline quaternary ammonium compounds that can be used as cleaning agents include tetramethylammonium hydroxide and tetraethylammonium hydroxide.

また本発明によれば、上記目的を達成するため、非金属
で構成された強アルカリ性化学物質からなる洗浄剤を供
給する第1の手段と、前記第1の手段からの洗浄剤によ
り放射性固体汚染物質の付着した汚染物質を洗浄する第
2の手段と、前記第2の手段で洗浄した後の廃院浄剤を
収容する第3の手段と、前記第3の手段に収容した廃院
浄剤を所定の温度まで加熱する第4の手段と、前記第4
の手段で加熱した結果、前記廃院浄剤より生じるガスを
排出する第5の手段とを含むことを特徴とする放射性固
体汚染物質の除染システムが提供される。
Further, according to the present invention, in order to achieve the above object, a first means for supplying a cleaning agent made of a strong alkaline chemical substance made of a nonmetal, and a cleaning agent from the first means are used to contaminate radioactive solids. a second means for cleaning pollutants to which substances have adhered; a third means for accommodating the waste hospital cleaning agent after cleaning by the second means; and a waste hospital cleaning agent stored in the third means a fourth means for heating to a predetermined temperature;
and a fifth means for discharging gas generated from the hospital cleaning agent as a result of heating by the means described above.

〔作用〕[Effect]

洗浄剤として強アルカリ性の第4級アンモニウム化合物
を使用して、固体金属表面に付着した有機酸性汚染物質
を強アルカリ性雰囲気下で分解し、酸性汚染物質中に含
有される金属イオンを遊離させる。遊離した金属イオン
は、強アルカリ性雰囲気中で水酸化物イオンと反応し水
酸化物沈澱体に変化させることなく、第4級アンモニウ
ム化合物と錯形成反応を起こし、錯体を生成する。この
錯体の生成により有機酸性汚染物質が洗浄される。
A strongly alkaline quaternary ammonium compound is used as a cleaning agent to decompose organic acidic contaminants adhering to solid metal surfaces in a strongly alkaline atmosphere, thereby liberating metal ions contained in the acidic contaminants. The liberated metal ions react with hydroxide ions in a strongly alkaline atmosphere to cause a complex-forming reaction with the quaternary ammonium compound to produce a complex without changing into a hydroxide precipitate. The formation of this complex cleanses organic acidic contaminants.

一方、このとき、洗浄剤としての第4級アンモニウム化
合物は非金属であるので、除染後の廃洗浄剤中に無機塩
は生成されず、廃洗浄剤中に含まれる含塩成分の低減化
が図れる。このため、濃縮により無機塩が沈澱する可能
性はなくなるので、廃院浄剤の大幅な減容が可能であり
、廃棄物発生量を大幅に減少できる。
On the other hand, at this time, since the quaternary ammonium compound used as a cleaning agent is a non-metal, inorganic salts are not generated in the waste cleaning agent after decontamination, and the salt-containing components contained in the waste cleaning agent are reduced. can be achieved. Therefore, there is no possibility that inorganic salts will precipitate due to concentration, so the volume of the hospital cleaning agent can be significantly reduced, and the amount of waste generated can be significantly reduced.

〔実施例〕〔Example〕

以下、本発明の一実施例を第1図及び第2図により説明
する。
An embodiment of the present invention will be described below with reference to FIGS. 1 and 2.

第1図において、本実施例の除染システムは、洗浄剤を
供給するための洗浄剤タンク1と、洗浄剤タンク1から
の洗浄剤により汚染物質2を洗浄する除染用タンク3と
、除染用タンク3で洗浄した後の廃洗浄剤を収容する廃
洗浄剤槽4と、廃洗浄剤槽4に収容した廃洗浄剤を所定
の温度まで加熱する電気炉5と、電気炉5で加熱した結
果、廃洗浄剤より生じるガスを排出するベントライン6
と、除染用タンク3内の除染剤を撹拌する撹拌機7と、
ベントライン6より排出されるガス中の放射性物質を除
去するベントフィルター8と、弁9゜10、ilとから
なっている。
In FIG. 1, the decontamination system of this embodiment includes a cleaning agent tank 1 for supplying a cleaning agent, a decontamination tank 3 for cleaning pollutants 2 with the cleaning agent from the cleaning agent tank 1, and a decontamination tank 3 for cleaning contaminants 2 with the cleaning agent from the cleaning agent tank 1. A waste cleaning agent tank 4 that stores the waste cleaning agent after washing in the dyeing tank 3, an electric furnace 5 that heats the waste cleaning agent stored in the waste cleaning agent tank 4 to a predetermined temperature, and heating in the electric furnace 5. Vent line 6 discharges gas generated from waste cleaning agent as a result of
and a stirrer 7 that stirs the decontamination agent in the decontamination tank 3;
It consists of a vent filter 8 for removing radioactive substances in gas discharged from a vent line 6, and valves 9, 10, and 11.

汚染物質2は、例えば、ルテニウムRu、ジルコニウム
Zr、ウランU等の放射性核種を含む有機溶媒が固体金
属表面に付着したものであり、洗浄剤は、強アルカリ性
第4級アンモニウム化合物として水酸化テトラメチルア
ンモニウムN (CH3)、ioHを使用している。
Contaminant 2 is, for example, organic solvent containing radionuclides such as ruthenium Ru, zirconium Zr, and uranium U attached to the solid metal surface, and the cleaning agent is tetramethyl hydroxide as a strong alkaline quaternary ammonium compound. Ammonium N (CH3) and ioH are used.

まず、除染用タンクに汚染物質2を入れ、次に弁9を開
いて洗浄剤タンク1より水酸化テトラメチルアンモニウ
ムを除染用タンク3に送り込み、撹拌機7で撹拌しなが
ら汚染物質2を洗浄剤中に数分間浸しておく。
First, put the pollutant 2 into the decontamination tank, then open the valve 9 to send tetramethylammonium hydroxide from the cleaning agent tank 1 into the decontamination tank 3, and add the pollutant 2 while stirring with the stirrer 7. Let it soak in the cleaning solution for a few minutes.

除染後、弁10を開き、廃洗浄剤を廃洗浄剤槽4へ送り
出し、廃洗浄剤槽4の周囲から電気炉5により加熱し、
廃洗浄剤を加熱減容する。このとき弁11を開けておき
、廃洗浄剤の加熱減容により発生したガスはベントフィ
ルター8を経てベントライン6より糸外に排出される。
After decontamination, the valve 10 is opened, the waste cleaning agent is sent to the waste cleaning agent tank 4, and the waste cleaning agent is heated from around the waste cleaning agent tank 4 by the electric furnace 5.
Heat the waste cleaning agent to reduce its volume. At this time, the valve 11 is kept open, and the gas generated by heating and reducing the volume of the waste cleaning agent is discharged from the vent line 6 through the vent filter 8 to the outside of the thread.

加熱減容後の廃液は例えばガラス固化処理により固形状
の廃棄物にされ、放射性廃棄物として所定の場所に保管
される。
The waste liquid after volume reduction by heating is converted into solid waste by, for example, vitrification treatment, and stored in a predetermined location as radioactive waste.

本実施例による除染効果の実験例を第2図に示す。この
実験例において、洗浄剤及び汚染物質2としてはそれぞ
れ上述した水酸化テトラメチルアンモニウム及びルテニ
ウムRu、ジルコニウムZr1ウランUの放射性核種を
含む有機溶媒か金属表面に付着したものを使用した。ま
た、放射性核種の濃度は、ルテニウムRuO,01mo
A! /I 。
FIG. 2 shows an experimental example of the decontamination effect of this example. In this experimental example, the cleaning agent and the contaminant 2 used were organic solvents containing the above-mentioned radionuclides of tetramethylammonium hydroxide, ruthenium Ru, zirconium Zr1, and uranium U, respectively, or those attached to the metal surface. In addition, the concentration of radionuclides is ruthenium RuO,01mo
A! /I.

ジルコニウムZ r 0. 1 m oA / n z
ウラ:/U O。
Zirconium Z r 0. 1 m oA / n z
Back: /U O.

002mol/Ilとした。水酸化テトラメチルアンモ
ニウムの濃度をパラメータと1.てそれぞれの洗浄率を
求め、第2図の横軸にその濃度をとり、縦軸に洗浄率を
とった。
002 mol/Il. The concentration of tetramethylammonium hydroxide is a parameter and 1. In FIG. 2, the horizontal axis represents the concentration, and the vertical axis represents the cleaning rate.

第2図に示すように、各元素に対して良好な除染性能が
得られ、いずれも98%以上の除染効率が得られること
が明らかとなった。
As shown in FIG. 2, it was revealed that good decontamination performance was obtained for each element, and decontamination efficiency of 98% or more was obtained for each element.

また、除染後に発生する廃棄物発生量については、一般
に用いられている化学的除染方法においては、例えば1
.00m3の廃洗浄剤が発生する場合、約160kgの
無機塩を生じる。この無機塩の沈澱を生じることは濾過
工程、脱水工程等の後続プロセスを必要とするので、無
機塩が沈澱しない程度に蒸発濃縮が制限される。これに
対I7、本実施例では水酸化テトラメチルアンモニウム
は非金属で無機塩を生じないので、このような制限はな
いので大幅な加熱減容が可能である。
In addition, regarding the amount of waste generated after decontamination, for example, 1
.. If 00 m3 of waste cleaning agent is generated, approximately 160 kg of inorganic salts are produced. Since precipitation of this inorganic salt requires subsequent processes such as filtration and dehydration, evaporative concentration is limited to the extent that the inorganic salt does not precipitate. On the other hand, in this example, tetramethylammonium hydroxide is a non-metal and does not form an inorganic salt, so there is no such restriction and the volume can be significantly reduced by heating.

水酸化テトラメチルアンモニウムを洗浄剤として用いた
場合の廃洗浄剤の加熱減容の方法としては、常圧下の蒸
溜する方法、所定の温度で熱分解を行う方法、白金系(
Pt(白金)、Pa(パラジウム)等)の触媒を用いる
酸化処理により熱分解し、無機ガス化する方法等がある
。本実施例において、廃洗浄剤を常圧下で蒸溜した場合
は上記従来の濃縮後の廃液量に比較して約1/12の容
積に濃縮できた。即ち、廃棄物発生量を従来に比較して
約1/12に低減することが可能となる。
When tetramethylammonium hydroxide is used as a cleaning agent, methods for heating and reducing the volume of the waste cleaning agent include distillation under normal pressure, thermal decomposition at a predetermined temperature, and platinum-based (
There is a method of thermally decomposing it by oxidation treatment using a catalyst such as Pt (platinum), Pa (palladium), etc., and converting it into an inorganic gas. In this example, when the waste cleaning agent was distilled under normal pressure, it could be concentrated to about 1/12 the volume of the waste liquid after concentration in the conventional method. That is, it is possible to reduce the amount of waste generated to about 1/12 compared to the conventional method.

また、約210℃程度で熱分解を行った場合は約1/1
1に減容でき、さらに白金系(Pt(白金)、Pa(パ
ラジウム)等)の触媒を用いる酸化方法により約300
℃で熱分解し、無機ガス化できた。
In addition, when thermal decomposition is performed at approximately 210℃, approximately 1/1
The volume can be reduced to about 300% by an oxidation method using a platinum-based catalyst (Pt (platinum), Pa (palladium), etc.).
It was thermally decomposed at ℃ and turned into an inorganic gas.

以上のように本実施例によれば1、無機塩を生成するこ
とがないため廃洗浄剤の大幅な減容が可能であり、廃棄
物発生量を著しく削減できる。また、生成した塩を処理
する濾過工程、脱水工程等の後続プロセスを必要とせず
、設備の合理化も可能となる。
As described above, according to this embodiment, 1. Since no inorganic salt is generated, the volume of waste cleaning agent can be significantly reduced, and the amount of waste generated can be significantly reduced. Further, there is no need for subsequent processes such as a filtration process and a dehydration process for treating the generated salt, making it possible to rationalize equipment.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、洗浄剤として非金属で構成された強ア
ルカリ性の第4級アンモニウム化合物を用いるので、除
染後の廃洗浄剤中に無機塩が生成されず、固体金属表面
の除染を十分に担保したまま、廃棄物発生量を大幅に低
減できる。
According to the present invention, since a strongly alkaline quaternary ammonium compound made of nonmetal is used as a cleaning agent, inorganic salts are not generated in the waste cleaning agent after decontamination, and solid metal surfaces can be decontaminated. It is possible to significantly reduce the amount of waste generated while maintaining sufficient security.

また、廃棄物中に無機塩が含まれないので、無機塩が発
生した場合に伴う後続プロセス(濾過工程、脱水工程等
)が不要となり、設備の合理化が可能となる。
Furthermore, since the waste does not contain inorganic salts, subsequent processes (filtration process, dehydration process, etc.) associated with the generation of inorganic salts are no longer necessary, and equipment can be rationalized.

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

第1図は本発明の一実施例による除染システムの概略図
であり、第2図はその除染システムを用いた行った除染
例を示す図である。 符号の説明 1・・・洗浄剤タンク(第1の手段) 2・・・汚染物質 3・・・除染用タンク(第2の手段) 4・・・廃洗浄剤槽(第3の手段) 5・・・電気炉(第4の手段) 6・・・ベントライン(第5の手段) a願人  株式会社 日立製作所 6・・・ベントライン(第5の手段)
FIG. 1 is a schematic diagram of a decontamination system according to an embodiment of the present invention, and FIG. 2 is a diagram showing an example of decontamination performed using the decontamination system. Explanation of symbols 1... Cleaning agent tank (first means) 2... Contaminant 3... Decontamination tank (second means) 4... Waste cleaning agent tank (third means) 5... Electric furnace (fourth means) 6... Vent line (fifth means) Applicant a Hitachi, Ltd. 6... Vent line (fifth means)

Claims (3)

【特許請求の範囲】[Claims] (1)放射性固体汚染物質の付着した固体金属表面の洗
浄剤として強アルカリ性の第4級アンモニウム化合物を
用いて洗浄し、洗浄後の廃洗浄剤を加熱分解して減容す
ることを特徴とする放射性固体汚染物質の除染方法。
(1) The method is characterized in that a strong alkaline quaternary ammonium compound is used as a cleaning agent to clean the solid metal surface to which radioactive solid contaminants have adhered, and the waste cleaning agent after cleaning is thermally decomposed to reduce its volume. Decontamination methods for radioactive solid contaminants.
(2)請求項1記載の放射性固体汚染物質の除去方法に
おいて、前記強アルカリ性の第4級アンモニウム化合物
が水酸化テトラメチルアンモニウムであることを特徴と
する放射性固体汚染物質の除染方法。
(2) The method for decontaminating radioactive solid contaminants according to claim 1, wherein the strongly alkaline quaternary ammonium compound is tetramethylammonium hydroxide.
(3)非金属で構成された強アルカリ性化学物質からな
る洗浄剤を供給する第1の手段と、前記第1の手段から
の洗浄剤により放射性固体汚染物質の付着した汚染物質
を洗浄する第2の手段と、前記第2の手段で洗浄した後
の廃洗浄剤を収容する第3の手段と、前記第3の手段に
収容した廃洗浄剤を所定の温度まで加熱する第4の手段
と、前記第4の手段で加熱した結果、前記廃洗浄剤より
生じるガスを排出する第5の手段とを含むことを特徴と
する放射性固体汚染物質の除染システム。
(3) a first means for supplying a cleaning agent made of a strong alkaline chemical substance made of non-metal; and a second means for cleaning contaminants to which radioactive solid contaminants have adhered using the cleaning agent from the first means; a third means for accommodating the waste cleaning agent after cleaning by the second means; and a fourth means for heating the waste cleaning agent contained in the third means to a predetermined temperature; and a fifth means for discharging gas generated from the waste cleaning agent as a result of heating by the fourth means.
JP15299090A 1990-06-12 1990-06-12 Method and apparatus for decontaminating radioactive solid contaminant Pending JPH0450699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15299090A JPH0450699A (en) 1990-06-12 1990-06-12 Method and apparatus for decontaminating radioactive solid contaminant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15299090A JPH0450699A (en) 1990-06-12 1990-06-12 Method and apparatus for decontaminating radioactive solid contaminant

Publications (1)

Publication Number Publication Date
JPH0450699A true JPH0450699A (en) 1992-02-19

Family

ID=15552552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15299090A Pending JPH0450699A (en) 1990-06-12 1990-06-12 Method and apparatus for decontaminating radioactive solid contaminant

Country Status (1)

Country Link
JP (1) JPH0450699A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2739216A1 (en) * 1995-09-22 1997-03-28 Commissariat Energie Atomique METHOD OF TREATING METALLIC ALUMINUM-BASED FUELS AND / OR NUCLEAR TARGETS WITH TETRAMETHYLAMMONIUM HYDROXIDE SOLUTIONS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2739216A1 (en) * 1995-09-22 1997-03-28 Commissariat Energie Atomique METHOD OF TREATING METALLIC ALUMINUM-BASED FUELS AND / OR NUCLEAR TARGETS WITH TETRAMETHYLAMMONIUM HYDROXIDE SOLUTIONS

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