JP3315510B2 - Molybdenum container decontamination method - Google Patents
Molybdenum container decontamination methodInfo
- Publication number
- JP3315510B2 JP3315510B2 JP03233694A JP3233694A JP3315510B2 JP 3315510 B2 JP3315510 B2 JP 3315510B2 JP 03233694 A JP03233694 A JP 03233694A JP 3233694 A JP3233694 A JP 3233694A JP 3315510 B2 JP3315510 B2 JP 3315510B2
- Authority
- JP
- Japan
- Prior art keywords
- molybdenum
- container
- nuclear fuel
- molybdenum container
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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- Manufacture And Refinement Of Metals (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は二酸化ウランペレットの
ような核燃料ペレットの焼成に使用したモリブデン容器
からウラン等の核燃料物質を除去するモリブデン容器の
除染方法に関する。更に詳しくは乾式バッチ処理法によ
るモリブデン容器の除染方法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 for decontaminating a molybdenum container for removing nuclear fuel material such as uranium from a molybdenum container used for firing nuclear fuel pellets such as uranium dioxide pellets. More specifically, the present invention relates to a method of decontaminating a molybdenum container by a dry batch processing method.
【0002】[0002]
【従来の技術】核燃料用の二酸化ウランペレットは、高
温におけるウラン化合物との両立性、耐熱性、焼成雰囲
気中の水素に対する安定性、価格等の観点から、金属モ
リブデン容器に入れて焼成される。この容器は焼成時に
長時間高温で加熱されるため、容器表面だけでなく容器
内部までウランが拡散侵入して汚染されている。従来、
このモリブデン容器からウランの除去する方法が特公昭
59−33877号公報、特開昭62−182699号
公報に提案されている。特公昭59−33877号公報
の除染方法は、モリブデン容器を陽極とし、特定の電解
質の溶液中で電解酸化処理して容器表面を酸化し、生成
する泥状酸化物層を分離する方法である。また特開昭6
2−182699号公報の除染方法は、汚染物質が付着
しているモリブデン容器を電解洗浄した後にこれを上記
汚染物質に対する貧溶媒中で超音波洗浄する方法であ
る。しかし、上記従来の2つの除染方法は、電解による
化学的湿式法であるため、電解質の溶液を必要とするば
かりでなく、電解により種々の廃液を生じ、その廃液処
理を要する。この種の廃液処理は複雑で処理コストが多
くかかる問題点があった。また上記特公昭59−338
77号公報に示される除染方法の除染係数は40〜30
0程度であって、除染係数が比較的低い不具合があっ
た。2. Description of the Related Art Uranium dioxide pellets for nuclear fuel are fired in a metal molybdenum container from the viewpoints of compatibility with uranium compounds at high temperatures, heat resistance, stability against hydrogen in a firing atmosphere, and price. Since this container is heated at a high temperature for a long time during sintering, uranium diffuses not only on the surface of the container but also into the inside of the container and is contaminated. Conventionally,
Methods for removing uranium from this molybdenum container have been proposed in Japanese Patent Publication No. 33877/1984 and Japanese Patent Application Laid-Open No. 62-182699. The decontamination method disclosed in JP-B-59-33877 is a method in which a molybdenum container is used as an anode, the surface of the container is oxidized by electrolytic oxidation treatment in a specific electrolyte solution, and a generated muddy oxide layer is separated. . See also
The decontamination method disclosed in Japanese Patent Application Laid-Open No. 2-182699 is a method in which a molybdenum container to which a contaminant is adhered is subjected to electrolytic cleaning and then ultrasonically cleaned in a poor solvent for the contaminant. However, since the above two conventional decontamination methods are chemical wet methods by electrolysis, not only an electrolyte solution is required, but also various waste liquids are generated by electrolysis, and the waste liquid treatment is required. This kind of waste liquid treatment has a problem that it is complicated and requires a large treatment cost. In addition, the above-mentioned Japanese Patent Publication No.
The decontamination coefficient of the decontamination method shown in JP-A-77 is 40 to 30.
It was about 0, and the decontamination coefficient was relatively low.
【0003】この点を解決するため、本出願人は電解に
よる種々の廃液を発生することなく、乾式法によりモリ
ブデン容器から核燃料物質を連続的にかつ確実に分離し
て、モリブデン容器を再生し、かつ核燃料物質を回収す
る不純物含有核燃料物質等の処理装置を開示した(特開
昭63−45594)。この処理装置は、不純物含有核
燃料物質又は核燃料物質含有材料を収容した容器(例え
ば、モリブデン容器)を一端の入口から他端の出口に通
過可能に形成された両端開放型の加熱炉と、この加熱炉
の両端の入口及び出口より酸化雰囲気ガスを同時に導入
する手段と、加熱炉の中間部に設けられ酸化雰囲気ガス
を加熱炉内で加熱によって不純物含有核燃料物質又は核
燃料物質含有材料からそれぞれ選択的に蒸発する不純物
酸化物又は材料酸化物とともに導出する導出管とを備え
る。In order to solve this problem, the present applicant has continuously and reliably separated nuclear fuel material from a molybdenum container by a dry method without generating various waste liquids by electrolysis, and regenerated the molybdenum container. In addition, an apparatus for treating nuclear fuel material containing impurities for recovering nuclear fuel material has been disclosed (JP-A-63-45594). The processing apparatus includes an open-ended heating furnace configured to allow a container (for example, a molybdenum container) containing an impurity-containing nuclear fuel material or a nuclear fuel material-containing material to pass from an inlet at one end to an outlet at the other end. Means for simultaneously introducing an oxidizing atmosphere gas from inlets and outlets at both ends of the furnace, and an oxidizing atmosphere gas provided at an intermediate portion of the heating furnace, which is selectively heated from the impurity-containing nuclear fuel material or the nuclear fuel material-containing material by heating in the heating furnace. A discharge pipe for discharging together with the impurity oxide or the material oxide that evaporates.
【0004】[0004]
【発明が解決しようとする課題】しかし、上記処理装置
は、両端が開放されている構造の加熱炉内で不純物酸化
物、材料酸化物及び核燃料物質を容器から完全に分離す
るために、加熱炉をこれらの融点以上の極めて高温、例
えば900℃まで昇温して、これらを蒸発又は気化させ
る必要があり、処理時間が長くなり、熱エネルギを多量
に消費する不具合があった。However, the above-mentioned processing apparatus has a heating furnace for completely separating impurity oxides, material oxides and nuclear fuel material from a container in a heating furnace having both ends open. Must be heated to an extremely high temperature above their melting point, for example, 900 ° C., to evaporate or vaporize them, resulting in a long processing time and a large amount of heat energy.
【0005】本発明の目的は、乾式バッチ処理法により
簡便で比較的少ない熱エネルギで短時間にかつ比較的高
い除染係数でウラン等の核燃料物質を除去するモリブデ
ン容器の除染方法を提供することにある。An object of the present invention is to provide a method for decontaminating a molybdenum container which can remove nuclear fuel materials such as uranium in a short time with a relatively small heat energy and with a relatively high decontamination coefficient by a dry batch processing method. It is in.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に、図1に示すように、本発明の除染方法は、核燃料ペ
レット焼成に使用したモリブデン容器14を給気口11
及び排気口12を有する密閉型の電気炉10に入れ、こ
の電気炉10内に給気口11から酸化力のあるエアを供
給しながらかつ排気口12から電気炉10内のエアを排
出しながら600〜620℃で0.75〜2時間モリブ
デン容器14を加熱し、加熱したモリブデン容器14を
少なくとも室温まで冷却した後、モリブデン容器14の
表面に析出した核燃料酸化物を研磨又は水洗により除去
する方法である。In order to achieve the above-mentioned object, as shown in FIG. 1, the decontamination method of the present invention uses a molybdenum container 14 used for burning nuclear fuel pellets in an air supply port 11.
Into the electric furnace 10 having a closed end and an exhaust port 12, while supplying oxidizing air from the air supply port 11 into the electric furnace 10 and discharging air from the electric furnace 10 from the exhaust port 12. A method of heating the molybdenum container 14 at 600 to 620 ° C. for 0.75 to 2 hours, cooling the heated molybdenum container 14 to at least room temperature, and removing the nuclear fuel oxide deposited on the surface of the molybdenum container 14 by polishing or washing with water. It is.
【0007】加熱温度が600℃未満であるか、又は加
熱時間が0.75時間未満では汚染物質のモリブデン容
器内部での表面への移動が少なく、620℃を越える
か、又は2時間を越えると、汚染物質が蒸発又は気化
し、その後の捕集が困難で複雑化する。冷却温度が50
℃以上では容器表面に核燃料酸化物が出現しにくい。モ
リブデン容器の表面から効率良く核燃料酸化物を析出さ
せるために、加熱時にはモリブデン容器を10〜20℃
/分の速度で昇温し、冷却時には電気炉の中で又は電気
炉から取出した後、モリブデン容器を25〜30℃/分
の速度で降温することが好ましい。具体的な温度、時
間、昇温速度及び降温速度は上記範囲の中で電気炉の容
量、モリブデン容器の容積、供給されるエアの酸化力等
に応じて適宜決められる。If the heating temperature is less than 600 ° C. or the heating time is less than 0.75 hours, the transfer of contaminants to the surface inside the molybdenum container is small, and if it exceeds 620 ° C. or exceeds 2 hours. The contaminants evaporate or evaporate, making subsequent collection difficult and complicated. Cooling temperature is 50
Above ° C, nuclear fuel oxides are unlikely to appear on the container surface. In order to efficiently deposit nuclear fuel oxide from the surface of the molybdenum container, the molybdenum container is heated at 10 to 20 ° C. during heating.
It is preferable that the molybdenum container be cooled at a rate of 25 to 30 ° C./min after the temperature is increased at a rate of 25 to 30 ° C./min. The specific temperature, time, heating rate, and cooling rate are appropriately determined in the above ranges according to the capacity of the electric furnace, the capacity of the molybdenum container, the oxidizing power of the supplied air, and the like.
【0008】[0008]
【作用】核燃料ペレット焼成に使用したモリブデン容器
14を酸化力のあるエアを供給しながら600〜620
℃で0.75〜2時間加熱すると、内部までウラン等の
核燃料物質が拡散侵入した汚染モリブデン容器14の表
面にU3O8,MoO3等の核燃料酸化物を含む酸化物が
出現する。この容器表面に核燃料酸化物が出現するの
は、加熱により容器内部のUO2がU3O8に変わり、こ
の酸化現象により容器表面に移行するものと考えられ
る。容器表面に出現した核燃料酸化物は上記温度が核燃
料酸化物の融点より低いため蒸発又は気化せず、冷却に
よりスケールとなって析出する。このスケールは研磨又
は水洗により除去される。The molybdenum container used for firing nuclear fuel pellets is supplied with oxidizing air for 600 to 620 minutes.
When heated at 0.75 ° C. for 0.75 to 2 hours, oxides containing nuclear fuel oxides such as U 3 O 8 and MoO 3 appear on the surface of the contaminated molybdenum container 14 into which the nuclear fuel material such as uranium diffuses and enters. It is considered that the nuclear fuel oxide appears on the surface of the container because UO 2 in the container is changed to U 3 O 8 by heating and is transferred to the surface of the container by this oxidation phenomenon. Since the above-mentioned temperature is lower than the melting point of the nuclear fuel oxide, the nuclear fuel oxide that has appeared on the container surface does not evaporate or evaporate, but precipitates as a scale upon cooling. This scale is removed by polishing or washing with water.
【0009】[0009]
【実施例】次に、本発明の実施例を図面に基づいて詳し
く説明する。図1に示すように、バッチ式マッフル炉で
ある電気炉10には給気口11と排気口12が設けら
れ、これらの給気口11と排気口12の間には開閉扉1
3が設けられる。電気炉10は給気口11及び排気口1
2を除いて密閉される構造になっている。電気炉10の
内部には核燃料ペレット焼成に使用したモリブデン容器
14を載せる台15が配置される。給気口11には酸素
に富んだエアを供給するためのエア管16が接続され、
排気口12にはエア管17が接続される。エア管17は
トラップ18のエア導入口19に接続される。トラップ
18のリッド18aにはエア導出管21が貫通して設け
られ、この導出管21はエア管22を介してフィルタ2
3の一端に接続される。フィルタ23の他端は排気管2
4に接続される。Next, an embodiment of the present invention will be described in detail with reference to the drawings. As shown in FIG. 1, an electric furnace 10 which is a batch type muffle furnace is provided with a supply port 11 and an exhaust port 12, and an opening / closing door 1 is provided between the supply port 11 and the exhaust port 12.
3 are provided. The electric furnace 10 has an inlet 11 and an outlet 1
With the exception of 2, the structure is sealed. A table 15 on which the molybdenum container 14 used for burning nuclear fuel pellets is placed inside the electric furnace 10. An air pipe 16 for supplying air rich in oxygen is connected to the air supply port 11,
An air pipe 17 is connected to the exhaust port 12. The air pipe 17 is connected to an air inlet 19 of a trap 18. An air outlet pipe 21 is provided through the lid 18 a of the trap 18, and the outlet pipe 21 is connected to the filter 2 through an air pipe 22.
3 is connected to one end. The other end of the filter 23 is the exhaust pipe 2
4 is connected.
【0010】次に、この除染装置を用いてモリブデン容
器14を除染する方法について説明する。先ず、使用済
みの2つのモリブデン容器14を用意した。放射能汚染
濃度は1つのモリブデン容器は4Bq(Becquerel)、他
のモリブデン容器は25Bqであった。電気炉10の開
閉扉13を開けて、これらのモリブデン容器14を台1
5の上に載せた後、開閉扉13を閉め、電気炉10内を
昇温した。この例ではエア管16から給気口11を介し
て25℃の新鮮な酸素に富んだエアを10リットル/分
の割合で供給しながら、室温から10〜20℃/分の速
度で610℃まで昇温し、そこで1.5時間維持した。
610℃の温度はウラン等の核燃料物質の酸化物の蒸発
又は気化温度(約800℃)より低いため、ウラン等の
核燃料物質の酸化物蒸気は殆ど発生しない。Next, a method for decontaminating the molybdenum container 14 using the decontamination apparatus will be described. First, two used molybdenum containers 14 were prepared. The radioactive contamination concentration was 4 Bq (Becquerel) for one molybdenum container and 25 Bq for the other molybdenum containers. The door 13 of the electric furnace 10 is opened, and these molybdenum containers 14
After being placed on 5, the opening and closing door 13 was closed, and the inside of the electric furnace 10 was heated. In this example, from room temperature to 610 ° C. at a rate of 10 to 20 ° C./min while supplying fresh oxygen-rich air at 25 ° C. from the air pipe 16 through the air supply port 11 at a rate of 10 liter / min. The temperature was raised and maintained there for 1.5 hours.
Since the temperature of 610 ° C. is lower than the evaporation or vaporization temperature (about 800 ° C.) of the oxide of the nuclear fuel material such as uranium, almost no oxide vapor of the nuclear fuel material such as uranium is generated.
【0011】排気口12から排出された電気炉10内の
加熱されたエアはエア管17を通って導入口19からト
ラップ18に導入される。ここでエアに含まれる極めて
微量のウラン等の核燃料物質の酸化物蒸気は冷却され、
固化して捕集される。トラップ18から排出されたエア
はエア管22を通ってフィルタ23を通過する。フィル
タ23では捕集し切れなかった酸化物粉塵が捕集され、
排気管24より浄化されたエアが排出される。The heated air in the electric furnace 10 discharged from the exhaust port 12 is introduced into a trap 18 through an inlet 19 through an air pipe 17. Here, very small amounts of oxide vapor of nuclear fuel substances such as uranium contained in the air are cooled,
Solidified and collected. The air discharged from the trap 18 passes through a filter 23 through an air pipe 22. The oxide dust that could not be collected by the filter 23 is collected,
The purified air is discharged from the exhaust pipe 24.
【0012】電気炉10で加熱された2つのモリブデン
容器14を電気炉10内で25〜30℃/分の速度で冷
却し、約400℃になったところで、開閉扉13を開け
て、電気炉10から取出し、室温下で冷却した。室温
(25℃)と同一温度になった2つのモリブデン容器1
4の表面にはスケールが形成された。ワイヤブラシで軽
く研磨するとスケールが剥離し、銀白色のモリブデン容
器となった。2つのモリブデン容器14の放射能濃度を
測定したところ、2つとも0.04Bqであった。これ
により1つのモリブデン容器の除染係数は100であ
り、他のモリブデン容器の除染係数は600であった。
剥離したスケールを分析したところ、U3O8,MoO3
等の核燃料酸化物を含む酸化物であった。The two molybdenum containers 14 heated in the electric furnace 10 are cooled in the electric furnace 10 at a rate of 25 to 30 ° C./min. Removed from 10 and cooled at room temperature. Two molybdenum containers 1 at the same temperature as room temperature (25 ° C.)
Scale was formed on the surface of No. 4. When lightly polished with a wire brush, the scale peeled off, resulting in a silver-white molybdenum container. When the radioactivity concentrations of the two molybdenum containers 14 were measured, both were found to be 0.04 Bq. Thereby, the decontamination coefficient of one molybdenum container was 100, and the decontamination coefficient of another molybdenum container was 600.
When the peeled scale was analyzed, U 3 O 8 , MoO 3
And the like containing nuclear fuel oxides.
【0013】[0013]
【発明の効果】以上述べたように、従来の湿式法に比べ
て、本発明の乾式法の除染方法は、電気炉による加熱で
済むため、廃液等の二次廃棄物が発生せず、しかも10
0〜600程度の比較的高い除染係数が得られる特長が
ある。また特開昭63−45594号公報に示される乾
式連続処理法に比べて、本発明の乾式バッチ処理法は電
気炉をモリブデン酸化物又は核燃料酸化物の融点以上に
加熱してこれらをモリブデン容器から完全に分離する必
要がなく、比較的少ない熱エネルギで短時間にかつ簡便
にウラン等の核燃料物質をモリブデン容器から除去で
き、処理コストが大幅に低減される。特に本発明の方法
は、バッチ処理であるため、少ない数の使用済みモリブ
デン容器の除染に好適である。As described above, the decontamination method of the dry method of the present invention requires only heating by an electric furnace as compared with the conventional wet method, so that no secondary waste such as waste liquid is generated. And 10
There is a feature that a relatively high decontamination coefficient of about 0 to 600 can be obtained. Compared with the dry continuous processing method disclosed in JP-A-63-45594, the dry batch processing method of the present invention heats the electric furnace to a temperature equal to or higher than the melting point of molybdenum oxide or nuclear fuel oxide and heats them from the molybdenum container. It is not necessary to completely separate the nuclear fuel material such as uranium from the molybdenum container in a short time and easily with relatively little heat energy, and the processing cost is greatly reduced. In particular, the method of the present invention is suitable for decontamination of a small number of used molybdenum containers because it is a batch process.
【図1】本発明の除染装置の構成図。FIG. 1 is a configuration diagram of a decontamination apparatus of the present invention.
10 電気炉 11 給気口 12 排気口 14 使用済みモリブデン容器 Reference Signs List 10 electric furnace 11 air supply port 12 exhaust port 14 used molybdenum container
フロントページの続き (72)発明者 甲斐 俊行 茨城県那珂郡東海村大字舟石川622番地 1 三菱原子燃料株式会社 東海製作所 内 (56)参考文献 特開 昭55−44917(JP,A) 特開 昭61−194397(JP,A) 特開 昭51−20900(JP,A) 特開 昭63−45594(JP,A) 特開 昭55−159200(JP,A) (58)調査した分野(Int.Cl.7,DB名) G21F 9/28 G21C 21/02 Continuation of the front page (72) Inventor Toshiyuki Kai 622, Funaiishikawa, Tokai-mura, Naka-gun, Ibaraki Prefecture 1 In the Tokai Works of Mitsubishi Nuclear Fuel Co., Ltd. (56) References JP-A-55-44917 (JP, A) 61-194497 (JP, A) JP-A-51-20900 (JP, A) JP-A-63-45594 (JP, A) JP-A-55-159200 (JP, A) (58) Fields investigated (Int. Cl. 7, DB name) G21F 9/28 G21C 21/02
Claims (2)
ン容器(14)を給気口(11)及び排気口(12)を有する密閉型
の電気炉(10)に入れ、 前記電気炉(10)内に前記給気口(11)から酸化力のあるエ
アを供給しながらかつ前記排気口(12)から前記電気炉(1
0)内のエアを排出しながら600〜620℃で0.75
〜2時間前記モリブデン容器(14)を加熱し、 前記加熱したモリブデン容器(14)を前記電気炉(10)から
取出して少なくとも室温まで冷却し、 前記モリブデン容器(14)の表面に析出した核燃料酸化物
を除去するモリブデン容器の除染方法。1. A molybdenum container (14) used for burning nuclear fuel pellets is placed in a closed electric furnace (10) having an air supply port (11) and an exhaust port (12). The electric furnace (1) is supplied from the air supply port (11) while supplying oxidizing air from the air supply port (11) and from the exhaust port (12).
0) 0.75 at 600 to 620 ° C while exhausting the air in
Heating the molybdenum container (14) for about 2 hours, removing the heated molybdenum container (14) from the electric furnace (10) and cooling it to at least room temperature, and oxidizing nuclear fuel deposited on the surface of the molybdenum container (14). Method of decontaminating molybdenum containers to remove material.
洗することにより酸化物を除去する請求項1記載のモリ
ブデン容器の除染方法。2. The method for decontaminating a molybdenum container according to claim 1, wherein the oxide is removed by polishing or washing the surface of the molybdenum container.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP03233694A JP3315510B2 (en) | 1994-03-02 | 1994-03-02 | Molybdenum container decontamination method |
Applications Claiming Priority (1)
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JP03233694A JP3315510B2 (en) | 1994-03-02 | 1994-03-02 | Molybdenum container decontamination method |
Publications (2)
Publication Number | Publication Date |
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JPH07244195A JPH07244195A (en) | 1995-09-19 |
JP3315510B2 true JP3315510B2 (en) | 2002-08-19 |
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JP03233694A Expired - Fee Related JP3315510B2 (en) | 1994-03-02 | 1994-03-02 | Molybdenum container decontamination method |
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JP (1) | JP3315510B2 (en) |
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1994
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JPH07244195A (en) | 1995-09-19 |
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