JPH0720292A - Method and facility for decontaminating metal waste - Google Patents
Method and facility for decontaminating metal wasteInfo
- Publication number
- JPH0720292A JPH0720292A JP16465193A JP16465193A JPH0720292A JP H0720292 A JPH0720292 A JP H0720292A JP 16465193 A JP16465193 A JP 16465193A JP 16465193 A JP16465193 A JP 16465193A JP H0720292 A JPH0720292 A JP H0720292A
- Authority
- JP
- Japan
- Prior art keywords
- decontamination
- metal waste
- dissolution
- liquid
- amount
- 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 And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、放射性物質により汚染
された金属廃棄物の表面を溶解することにより、表面に
付着している放射性物質を除去する金属廃棄物の除染方
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 an apparatus for decontaminating a metal waste by dissolving the surface of the metal waste contaminated with radioactive substances to remove the radioactive substances adhering to the surface. Is.
【0002】[0002]
【従来の技術】例えば原子力発電所の定期修理の際に発
生するステンレススチール製のパイプのような金属廃棄
物は、その表面に放射性物質が付着しているために廃棄
することができず、従来はそのままドラム缶に入れて保
管されている。しかしこのような方法では極めて大きい
保管スペースが必要となるため、その解決策が求められ
ている。2. Description of the Related Art A metal waste such as a pipe made of stainless steel, which is generated at the time of periodic repair of a nuclear power plant, cannot be discarded because radioactive substances adhere to the surface of the metal waste. Is stored in a drum as it is. However, such a method requires an extremely large storage space, and therefore a solution is required.
【0003】そこで本発明者は、放射性物質が付着して
いる金属廃棄物の表面を所要の深さまで溶解すれば、そ
の内部は一般廃棄物として取り扱えることを見いだし、
硝酸を主成分とする除染液を用いて除染を行う金属廃棄
物の除染方法を先に開発し、特許出願済みである。とこ
ろが従来は除染温度、除染時間等の条件を経験的に設定
し、金属廃棄物のサイズの大小に無関係に除染液中に浸
漬して除染を行っていたため、溶解厚さのバラツキが大
きく必要以上に表面を溶解したり、溶解厚さが不足する
ために十分な除染効果を達成できない等の問題があっ
た。Therefore, the present inventor has found that if the surface of a metal waste to which radioactive substances adhere is dissolved to a required depth, the inside can be handled as general waste,
A decontamination method for metallic waste, which uses a decontamination solution containing nitric acid as a main component for decontamination, was previously developed and a patent has been applied for. However, in the past, conditions such as decontamination temperature and decontamination time were set empirically, and decontamination was performed by immersing the metal waste in the decontamination liquid regardless of the size of the waste metal, and therefore the variation in the dissolution thickness was varied. However, there is a problem that the surface is unnecessarily dissolved and the dissolution thickness is insufficient, so that a sufficient decontamination effect cannot be achieved.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、除染条件を科学的に設定し、金属廃
棄物のサイズの大小にかかわらず常に安定した溶解厚さ
を達成することができるようにした金属廃棄物の除染方
法及び装置を提供するためになされたものである。The present invention solves the above-mentioned conventional problems, scientifically sets decontamination conditions, and always achieves a stable dissolution thickness regardless of the size of metal waste. The present invention has been made to provide a method and an apparatus for decontaminating a metal waste that can be performed.
【0005】[0005]
【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の金属廃棄物の除染方法は、除染液
により金属廃棄物の表面を溶解する金属廃棄物の除染方
法において、除染液による金属廃棄物の溶解量が飽和に
達する除染液温度及び溶解時間のもとに、溶解面積/除
染液量と溶解厚さとの関係式を予め求めておき、金属廃
棄物を形状認識してその表面積を計算し、これを前記の
関係式に代入することにより得られる所要の溶解厚さに
対応する除染液量で除染を行うことを特徴とするもので
ある。The method for decontaminating a metal waste of the present invention, which has been made to solve the above problems, is a method for decontaminating a metal waste by dissolving the surface of the metal waste with a decontamination solution. In, the relational expression of dissolution area / decontamination solution amount and dissolution thickness is obtained in advance based on the decontamination solution temperature and the dissolution time when the dissolution amount of the metal waste by the decontamination solution reaches saturation. It is characterized in that the shape of an object is recognized, its surface area is calculated, and this is substituted into the above-mentioned relational expression to perform decontamination with an amount of decontamination liquid corresponding to the required dissolution thickness. .
【0006】また上記の課題を解決するためになされた
本発明の金属廃棄物の除染装置は、除染室の入口側に設
けられた金属廃棄物の形状認識装置と、その認識結果に
基づいて金属廃棄物の表面積の算出及びその表面積を所
要の溶解厚さまで溶解するに必要な除染液量の算出とを
行う演算手段と、この演算手段により制御される除染槽
の液量制御手段とを備えたことを特徴とするものであ
る。A metal waste decontamination apparatus of the present invention made to solve the above-mentioned problems is based on the recognition result of the shape of the metal waste provided at the entrance side of the decontamination chamber. Calculating means for calculating the surface area of the metal waste and calculating the amount of the decontamination liquid necessary for dissolving the surface area to a required dissolution thickness, and the liquid volume control means for the decontamination tank controlled by the calculating means. It is characterized by having and.
【0007】[0007]
【作用】本発明によれば、除染室の入口側に設けられた
形状認識装置によって金属廃棄物の形状を認識し、表面
積を算出する。そして予め求めておいた除染液による金
属廃棄物の溶解量が飽和に達する除染液温度及び溶解時
間のもとにおける溶解面積/除染液量と溶解厚さとの関
係式に基づき、演算手段が所要の溶解厚さに対応する除
染液量を求め、それに応じて液量制御手段が除染槽の除
染液量を制御する。このために金属廃棄物をこの除染槽
において上記の除染液温度及び溶解時間のもとで除染す
れば、金属廃棄物は常に一定の厚さまで溶解されること
となり、必要以上に表面を溶解したり、溶解厚さが不足
するために十分な除染効果を達成できない等の問題を生
ずることがない。According to the present invention, the shape recognition device provided on the entrance side of the decontamination chamber recognizes the shape of the metal waste and calculates the surface area. Then, based on a relational expression of dissolution area / decontamination solution amount and dissolution thickness under the decontamination solution temperature and dissolution time at which the dissolution amount of the metal waste by the decontamination solution reaches saturation, which is previously calculated Determines the amount of decontamination liquid corresponding to the required dissolution thickness, and the liquid amount control means controls the amount of decontamination liquid in the decontamination tank in accordance therewith. For this reason, if the metal waste is decontaminated in this decontamination tank under the above-mentioned decontamination solution temperature and dissolution time, the metal waste will always be dissolved to a certain thickness, and the surface of the metal waste will be removed more than necessary. It does not cause problems such as dissolution or lack of sufficient dissolution thickness to achieve a sufficient decontamination effect.
【0008】[0008]
【実施例】以下に本発明を図示の実施例に基づいて更に
詳細に説明する。本発明においては、まず金属廃棄物の
溶解量が飽和に達する除染液温度及び溶解時間を求め
る。従来は常温付近において除染を行っていたために、
溶解量が溶解時間とともに徐々に増加して飽和に達する
に至らなかったのであるが、本発明では除染液の組成、
除染液温度、溶解時間を種々に変更することにより、比
較的短時間に溶解量が飽和に達する条件を把握した。The present invention will be described in more detail below with reference to the illustrated embodiments. In the present invention, first, the decontamination solution temperature and the dissolution time at which the amount of dissolved metal waste reaches saturation are determined. Conventionally, since decontamination was performed near room temperature,
Although the amount of dissolution did not reach saturation by gradually increasing with the dissolution time, in the present invention, the composition of the decontamination solution,
By changing the decontamination solution temperature and dissolution time variously, the conditions under which the dissolution amount reached saturation in a relatively short time were understood.
【0009】具体的には、本実施例で使用した除染液は
硝酸20重量部に対して、塩酸2重量部、弗酸3重量部を
混合した混酸であり、除染対象となる金属廃棄物として
ステンレススチール(SUS 304)を選択した。この場合、
図1に示すように除染液温度を従来よりも高い70℃とす
ると、溶解時間20分でほぼ飽和に達し、溶解時間を1時
間とすれば完全な飽和となる。なおここで80℃とすると
溶解量が減少するのは、蒸発により除染液の性能が低下
するためと考えられる。この結果から、上記の除染液に
ついては除染液温度を70℃とし、溶解時間を安全を見込
んで1時間とすれば、金属廃棄物の溶解量が完全な飽和
に達することが分かる。Specifically, the decontamination solution used in this example is a mixed acid prepared by mixing 2 parts by weight of hydrochloric acid and 3 parts by weight of hydrofluoric acid with 20 parts by weight of nitric acid. Stainless steel (SUS 304) was selected as the material. in this case,
As shown in FIG. 1, when the temperature of the decontamination solution is set to 70 ° C., which is higher than that of the conventional method, it reaches almost saturation in 20 minutes of dissolution time, and it becomes completely saturated in 1 hour of dissolution time. The reason why the dissolution amount decreases at 80 ° C. here is considered to be that the performance of the decontamination solution deteriorates due to evaporation. From this result, it can be seen that when the temperature of the decontamination solution is set to 70 ° C. and the dissolution time is set to 1 hour in consideration of safety, the dissolved amount of the metal waste reaches a complete saturation.
【0010】図2は上記の条件下における溶解面積/除
染液量と溶解厚さとの関係及び溶解面積/除染液量と金
属イオン濃度との関係を求めたグラフである。この図2
のグラフに示されるように、溶解面積/除染液量の値が
約0.07m2/Lを越えると溶解した金属イオン濃度は50〜60
g/L のレベルでほぼ一定となり、また溶解面積/除染液
量の値を変化させれば、金属廃棄物(ステンレススチー
ル)の溶解厚さを連続的に変化させることができること
が分かる。従って、金属廃棄物の溶解面積を事前に測定
して除染液量を調整すれば、任意の溶解厚さを得ること
が可能となる。なお従来得られている知見として、金属
廃棄物の表面から30μm を溶解すれば放射性物質は完全
に除去できることが分かっているため、図2のグラフか
ら溶解面積/除染液量の値を0.20m2/Lとすればよいこと
が確認できる。FIG. 2 is a graph showing the relationship between the dissolution area / amount of decontamination solution and the dissolution thickness and the relationship between the dissolution area / amount of decontamination solution and the metal ion concentration under the above conditions. This Figure 2
As shown in the graph, the dissolved metal ion concentration is 50 to 60 when the value of dissolved area / decontamination solution amount exceeds about 0.07 m 2 / L.
It can be seen that the solution thickness of the metal waste (stainless steel) can be continuously changed by changing the value of the dissolution area / decontamination solution amount to be almost constant at the level of g / L. Therefore, if the dissolved area of the metal waste is measured in advance and the amount of the decontamination solution is adjusted, an arbitrary dissolved thickness can be obtained. In addition, it has been found that radioactive substances can be completely removed by dissolving 30 μm from the surface of metal waste, so the graph of Fig. 2 shows that the value of dissolved area / decontamination solution amount is 0.20 m. It can be confirmed that 2 / L is enough.
【0011】図3は本発明を実施するための装置を示す
もので、除染室1の入口側に設けられた金属廃棄物の形
状認識装置2によって、金属廃棄物の形状を自動的に認
識し、マイクロコンピュータ等の演算手段3が金属廃棄
物の表面積を算出する。また演算手段3はこのようにし
て算出された金属廃棄物の表面積を、上記した図2に示
されたような溶解面積/除染液量と溶解厚さとの関係式
に代入し、金属廃棄物の表面を所要の溶解厚さまで溶解
するに必要な除染液量を算出する。FIG. 3 shows an apparatus for carrying out the present invention, in which the shape of the metal waste is automatically recognized by the shape recognizing device 2 for the metal waste provided at the entrance side of the decontamination chamber 1. Then, the calculation means 3 such as a microcomputer calculates the surface area of the metal waste. Further, the calculating means 3 substitutes the surface area of the metal waste calculated in this way into the relational expression between the dissolution area / the amount of the decontamination liquid and the dissolution thickness as shown in FIG. Calculate the amount of decontamination liquid required to dissolve the surface of to the required dissolution thickness.
【0012】一方、除染室1の内部の除染槽4には70℃
に保たれた前記の除染液が充填されているが、除染液の
再生を目的とした除染廃液処理装置5との間に除染液の
循環経路が形成されている。そこでこの循環経路に設け
られた液量制御手段6が、除染槽4の除染液量を演算手
段3による算出結果に基づいて制御する。このため、金
属廃棄物をこの除染槽4に浸漬して例えば1時間の除染
を行えば、一定厚さ (例えば30μm)を溶解することがで
きる。その後、金属廃棄物はクレーン9によりリンス槽
7、8でリンスされ、外部に取り出される。また放射性
物質を含有する除染液は、除染廃液処理装置5によって
再生処理される。このようにして除染された後の金属廃
棄物は放射線量をチェックされ、安全であることが確認
されれば一般廃棄物として処理することが可能となる。On the other hand, in the decontamination tank 4 inside the decontamination chamber 1, 70 ° C.
Although the decontamination liquid kept in the above condition is filled, a circulation route of the decontamination liquid is formed between the decontamination liquid and the decontamination waste liquid treatment device 5 for the purpose of regenerating the decontamination liquid. Therefore, the liquid amount control means 6 provided in this circulation path controls the decontamination liquid amount in the decontamination tank 4 based on the calculation result by the calculation means 3. Therefore, by immersing the metal waste in the decontamination tank 4 and performing decontamination for 1 hour, for example, a certain thickness (for example, 30 μm) can be dissolved. After that, the metal waste is rinsed in the rinse tanks 7 and 8 by the crane 9 and taken out to the outside. The decontamination liquid containing the radioactive substance is regenerated by the decontamination waste liquid treatment device 5. The metal waste that has been decontaminated in this way is checked for radiation dose, and if it is confirmed to be safe, it can be treated as general waste.
【0013】[0013]
【発明の効果】以上に説明したように、本発明の金属廃
棄物の除染方法によれば、金属廃棄物のサイズの大小に
かかわらず常に安定した溶解厚さで除染を行うことがで
き、過度に溶解することによる無駄や、溶解不足による
不完全な除染を防止することができる。また本発明の金
属廃棄物の除染装置によれば、上記の除染を自動的に行
うことができる。なお、実施例はステンレススチールを
溶解するに適した特定の組成の除染液についてのもので
あるが、金属廃棄物の種類や除染液の組成は特にこれに
限定されないことはいうまでもないことである。As described above, according to the method for decontaminating metal waste of the present invention, decontamination can always be performed with a stable dissolution thickness regardless of the size of the metal waste. It is possible to prevent waste due to excessive dissolution and incomplete decontamination due to insufficient dissolution. Further, according to the decontamination apparatus for metal waste of the present invention, the above decontamination can be automatically performed. It should be noted that the examples relate to the decontamination liquid having a specific composition suitable for dissolving stainless steel, but it goes without saying that the type of metal waste and the composition of the decontamination liquid are not particularly limited to this. That is.
【図1】溶解時間と溶解量との関係を示すグラフであ
る。FIG. 1 is a graph showing the relationship between dissolution time and dissolution amount.
【図2】溶解面積/除染液量と、溶解厚さ及び金属イオ
ン濃度との関係を示すグラフである。FIG. 2 is a graph showing the relationship between dissolution area / decontamination solution amount, dissolution thickness and metal ion concentration.
【図3】実施例の金属廃棄物の除染装置を示すブロック
図である。FIG. 3 is a block diagram showing a decontamination device for metallic waste of an embodiment.
1 除染室、2 形状認識装置、3 演算手段、6 液
量制御手段1 decontamination room, 2 shape recognition device, 3 calculation means, 6 liquid volume control means
Claims (2)
金属廃棄物の除染方法において、除染液による金属廃棄
物の溶解量が飽和に達する除染液温度及び溶解時間のも
とに、溶解面積/除染液量と溶解厚さとの関係式を予め
求めておき、金属廃棄物を形状認識してその表面積を計
算し、これを前記の関係式に代入することにより得られ
る所要の溶解厚さに対応する除染液量で除染を行うこと
を特徴とする金属廃棄物の除染方法。1. A method for decontaminating a metal waste by dissolving the surface of the metal waste with a decontamination solution, which is based on the decontamination solution temperature and the dissolution time at which the amount of the metal waste dissolved by the decontamination solution reaches saturation. In addition, the relational expression between dissolved area / decontamination solution amount and dissolved thickness is obtained in advance, the shape of metal waste is recognized, its surface area is calculated, and this is substituted into the above relational expression. A method for decontaminating metal waste, characterized in that decontamination is performed with an amount of decontamination liquid corresponding to the dissolved thickness of.
形状認識装置と、その認識結果に基づいて金属廃棄物の
表面積の算出及びその表面積を所要の溶解厚さまで溶解
するに必要な除染液量の算出とを行う演算手段と、この
演算手段により制御される除染槽の液量制御手段とを備
えたことを特徴とする金属廃棄物の除染装置。2. A device for recognizing the shape of a metal waste provided on the entrance side of a decontamination chamber, and calculating the surface area of the metal waste based on the recognition result and melting the surface area to a required dissolution thickness. An apparatus for decontaminating a metal waste, comprising: a calculation unit for calculating the amount of decontamination liquid and a liquid amount control unit for the decontamination tank controlled by the calculation unit.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05164651A JP3091349B2 (en) | 1993-07-02 | 1993-07-02 | Metal waste decontamination method and apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP05164651A JP3091349B2 (en) | 1993-07-02 | 1993-07-02 | Metal waste decontamination method and apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0720292A true JPH0720292A (en) | 1995-01-24 |
JP3091349B2 JP3091349B2 (en) | 2000-09-25 |
Family
ID=15797234
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP05164651A Expired - Fee Related JP3091349B2 (en) | 1993-07-02 | 1993-07-02 | Metal waste decontamination method and apparatus |
Country Status (1)
Country | Link |
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JP (1) | JP3091349B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002250793A (en) * | 2001-02-26 | 2002-09-06 | Teikoku Sen I Co Ltd | Decontamination equipment |
JP2014126490A (en) * | 2012-12-27 | 2014-07-07 | E&E Techno Service Co Ltd | Decontamination device |
-
1993
- 1993-07-02 JP JP05164651A patent/JP3091349B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002250793A (en) * | 2001-02-26 | 2002-09-06 | Teikoku Sen I Co Ltd | Decontamination equipment |
JP2014126490A (en) * | 2012-12-27 | 2014-07-07 | E&E Techno Service Co Ltd | Decontamination device |
Also Published As
Publication number | Publication date |
---|---|
JP3091349B2 (en) | 2000-09-25 |
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