JPH02201199A - Treatment of high-radioactive waste - Google Patents
Treatment of high-radioactive wasteInfo
- Publication number
- JPH02201199A JPH02201199A JP1922489A JP1922489A JPH02201199A JP H02201199 A JPH02201199 A JP H02201199A JP 1922489 A JP1922489 A JP 1922489A JP 1922489 A JP1922489 A JP 1922489A JP H02201199 A JPH02201199 A JP H02201199A
- Authority
- JP
- Japan
- Prior art keywords
- radioactive waste
- elements
- heating
- treatment
- highly radioactive
- 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.)
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Links
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21F—PROTECTION AGAINST X-RADIATION, GAMMA RADIATION, CORPUSCULAR RADIATION OR PARTICLE BOMBARDMENT; TREATING RADIOACTIVELY CONTAMINATED MATERIAL; DECONTAMINATION ARRANGEMENTS THEREFOR
- G21F9/00—Treating radioactively contaminated material; Decontamination arrangements therefor
- G21F9/28—Treating solids
- G21F9/30—Processing
- G21F9/32—Processing by incineration
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- High Energy & Nuclear Physics (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、使用済燃料の再処理工程等で発生する高放射
性廃棄物を高温で処理し、その加熱過程で各元素の各化
学形態における昇華又は沸騰現象を利用して各元素を分
離し、残渣を同化体として回収する高放射性廃棄物の処
理方法に関するものである。[Detailed Description of the Invention] [Field of Industrial Application] The present invention treats highly radioactive waste generated in spent fuel reprocessing processes at high temperatures, and in the heating process, the chemical forms of each element are This invention relates to a highly radioactive waste treatment method that uses sublimation or boiling phenomena to separate each element and recover the residue as an assimilate.
[従来の技術]
使用済核燃料の再処理に伴って発生ずる高放射性廃棄物
中には、長半減期の超ウラン元素やTc(テクネチウム
)、発熱の大部分を占めるため処理貯蔵処分においての
注目元素であるCs(セシウム)、Sr(ストロンチウ
ム)及び有用金属であるRh(ロジウム)、Pd(パラ
ジウム)等の白金族元素が含まれている。[Conventional technology] Highly radioactive waste generated during the reprocessing of spent nuclear fuel contains transuranium elements with long half-lives and Tc (technetium), which accounts for most of the heat generation and is therefore attracting attention in processing, storage and disposal. It contains platinum group elements such as elements Cs (cesium) and Sr (strontium) and useful metals Rh (rhodium) and Pd (palladium).
従って固化体として処理する前段階でこれらを分離回収
し、放射線源、発熱体、貴金属として利用することは、
資源の有効利用を図る上で極めで重要である。Therefore, it is important to separate and recover these materials before processing them as a solidified material and use them as radiation sources, heating elements, and precious metals.
This is extremely important in making effective use of resources.
高放射性廃棄物からこれらの元素を回収する従来技術と
しては次の3つの方法が知られている。それらは、
(j)再処理1稈で発生ずる高放射性廃棄物を、特殊な
1溶媒を用いて目的核種を分離する抽出分前法
:鎚iIj処理下程で発生する高放身・↑性廃棄物を、
イ(ンつマ(Q処理し、目的核種を分離するイオン交換
法
(■ガうスフ6融の際、鉛を添υ■し白金族元素を鉛I
Aに1.1% (’5させて分離するガラス固化工程に
おける白金族元素の鉛抽出法
である。The following three methods are known as conventional techniques for recovering these elements from highly radioactive waste. These are: (j) Pre-extraction method in which target nuclides are separated from the highly radioactive waste generated in one culm of reprocessing using a special solvent: Highly radioactive waste generated in the lower stage of the reprocessing process. waste,
Ion-exchange method to separate target nuclides through Q treatment
This is a lead extraction method for platinum group elements in the vitrification process in which A is separated by 1.1% ('5).
[発明が解決しようとする課8]
しかし」1記のような従来技術ではそれぞれ次のような
欠点がある。[Problem to be Solved by the Invention 8] However, each of the prior art techniques as described in Section 1 has the following drawbacks.
■抽出分離法では、再処理工程に新規溶媒を導入するた
め、溶媒処理工程が複雑化し、主抽出工程の効率が低下
する。■In the extraction separation method, a new solvent is introduced into the reprocessing process, which complicates the solvent treatment process and reduces the efficiency of the main extraction process.
■イオン交換法の場合には、イオン交換樹脂が硝酸と接
触することにより燃焼性物質が4に成するため安全性の
面で問題がある。(2) In the case of the ion exchange method, there is a problem in terms of safety because combustible substances are formed when the ion exchange resin comes into contact with nitric acid.
■ガラス固化工程における白金族元素の鉛抽出法では、
白金族元素の分離は可能であるが、白金ら父元素を単独
に抽出するためには二次処理が必要となる。■In the lead extraction method of platinum group elements in the vitrification process,
Although it is possible to separate platinum group elements, secondary treatment is required to extract platinum and other parent elements alone.
更にこれらの方法での問題は、どの方法を採用しても高
放射性廃棄物の1高減容処理を行うことができないこと
である。A further problem with these methods is that no matter which method is adopted, highly radioactive waste cannot be treated to reduce the volume of highly radioactive waste.
本発明の目的は、上記のような従来技術の欠点を解消し
、加熱処理という極く単純な工法によって有用元素の分
離回収を行うことができ、且つ二次廃棄物が発生せず、
また高減容固化体を得ることができる高放射性廃棄物の
処理方法を提供することにある。The purpose of the present invention is to eliminate the drawbacks of the prior art as described above, to be able to separate and recover useful elements using an extremely simple method of heat treatment, and to do so without generating secondary waste.
Another object of the present invention is to provide a method for treating highly radioactive waste that can yield a solidified material with a high volume reduction.
[課題を解決するための手段]
」1記の技術的課題を解決できる本発明は、高放射性廃
棄物を高温で加熱処理又は加熱還元処理し、一部の含有
元素を気化させて分翻し、冷却捕集する高放射性廃棄物
の処理方法である。[Means for Solving the Problems] The present invention, which can solve the technical problem described in 1. , a method of processing highly radioactive waste that involves cooling and collection.
高放射性廃棄物は、通常の場合、使用済核燃f4の再処
理工程における抽出残渣として得られる硝酸溶液であり
、使用済燃料中の殆ど全ての核分裂生成物、アクチニド
を含有している。本発明では、この硝酸溶液を加熱処理
し、水分及び硝酸を原発させて仮焼体を得、その仮焼体
を500〜3000℃、より好ましくは1000〜25
00℃に加熱処理する0例えば第1段階として酸化物の
化学形態で昇華又は沸騰する元素を常圧又は減圧下で加
熱処理することにより分h1シ2、各元素の化学形態の
昇華点又は沸点に対応した温度に設定した冷却捕集装置
で各元素を分離捕集する。次に第2段階として水素等の
1元処理剤を導入しつつ加熱処理することで高放射性物
質を還元し、金属の化学形態で沸騰又は昇華する元素を
分離し、第1段階と同様、各元素に対応した温度の冷却
捕集装置で分離回収する。勿論、第1段階での昇温過程
で金属化する元素は、第2段階での還元反応過程を経ず
に昇華沸騰処理し分離することが可能である。Highly radioactive waste is usually a nitric acid solution obtained as an extraction residue in the reprocessing process of spent nuclear fuel F4, and contains almost all the fission products and actinides in the spent fuel. In the present invention, this nitric acid solution is heat-treated to generate moisture and nitric acid to obtain a calcined body, and the calcined body is heated to 500 to 3000°C, more preferably 1000 to 25°C.
For example, as a first step, elements that sublimate or boil in their oxide chemical form are heat treated under normal pressure or reduced pressure to reduce the sublimation point or boiling point of each element's chemical form. Each element is separated and collected using a cooling collection device set at a temperature corresponding to the temperature. Next, in the second step, highly radioactive substances are reduced by heat treatment while introducing a single processing agent such as hydrogen, and elements that boil or sublimate in the chemical form of metal are separated, and as in the first step, each It is separated and collected using a cooling collection device with a temperature corresponding to the element. Of course, the elements metallized during the temperature raising process in the first stage can be separated by sublimation boiling treatment without going through the reduction reaction process in the second stage.
使用済燃料から放射性物質を除去する技術としてポロキ
シデージョン法があるが、これはクリプトン、ヨウ素、
トリチウムなど非金属元素を対象としているに過ぎない
。本発明は金属元素を対象としており、単に高レベル廃
棄物を高温に加熱して高沸点の放射性物質を除去するこ
とのみならず、還元反応を組み合わせることにより、処
分において問題となる高発熱量元素であるC、sとSr
の両者を除去可能となる。Poroxide duration is a technology for removing radioactive materials from spent fuel, but this method uses krypton, iodine,
It only targets non-metallic elements such as tritium. The present invention targets metal elements, and not only removes high-boiling point radioactive materials by simply heating high-level waste to high temperatures, but also combines reduction reactions with high-calorific elements that pose problems in disposal. C, s and Sr
Both can be removed.
回収後の残渣は金属又は金属と酸化物の混合体であり、
減容した高放射性同化体として回収できる。The residue after recovery is a metal or a mixture of metal and oxide,
It can be recovered as a highly radioactive assimilate with reduced volume.
「作用」
殆どの元素は他の元素と異なる沸点又は昇華点を有して
いる。高放射性廃棄物中に含まれている元素には、酸化
物あるいは金属の形態で比較的低い昇華点あるいは沸点
を有するものがある。例えば金属セシウムは690℃、
酸化テクネチウムは311℃、金属カドミウムは765
゛C,金属ストロンチウムは1384℃等の沸点を持−
つ、このことを利用することによって、高放射性廃棄物
を高温で処理し酸化物として、又は水素等で還元し金属
として、昇華又は沸騰さυ、これをそれぞれ所定の温度
で冷却することによりf↑用元素を各元素毎に分離回収
することう(できろ。``Action'' Most elements have boiling points or sublimation points that are different from other elements. Some elements contained in highly radioactive waste have relatively low sublimation or boiling points in the form of oxides or metals. For example, metal cesium is 690℃,
Technetium oxide is 311℃, metal cadmium is 765℃
゛C, metallic strontium has a boiling point of 1384℃ etc.
By taking advantage of this fact, highly radioactive waste can be treated at high temperatures to form oxides, or reduced with hydrogen etc. to form metals, sublimation or boiling υ, and cooling them at predetermined temperatures to produce f. ↑It is possible to separate and recover the elements for each element.
c S 、&びSrの除去により高放射性固体の発効¥
は杓1054となり、処分tこおける埋設密度は大幅に
向上する。因にCsのみの除去では発効噴は50%とな
るに過ぎず、大きな効果は期待できない、Srの酸化物
の沸点は少なくとも2430°C以上であり、金属S「
の沸点は前記のように1384℃であるから、本発明の
ように還元反応を組み合わせる方法によってはしめてス
トロンチウムを分離できる。Removal of cS, & Sr reduces the effectiveness of highly radioactive solids¥
1054, and the burial density in the disposal space is greatly improved. Incidentally, if only Cs is removed, the effective injection will be only 50%, and no great effect can be expected.The boiling point of Sr oxide is at least 2430°C or higher,
As mentioned above, the boiling point of strontium is 1384°C, so strontium can be separated by combining reduction reactions as in the present invention.
なお加熱処理又はカ■熱還元処理を減圧下で実施すると
更に低い温度で各元素の気化を行わせることができる。Note that by carrying out the heat treatment or the thermal reduction treatment under reduced pressure, each element can be vaporized at an even lower temperature.
[実ち桓例1
第1図は本発明方法の実施に用いる処理装置の一例を示
す概念図である。この処理装置は、加りき処理袋:ηl
Oと、それに連結される複数台の冷却捕集装置12a、
・・・、12nをINえている。加熱処理装置lOは、
加熱容器14と発熱体16等からなり、上部には処理ガ
スの供給口18が設けられ、また冷却捕集装置!2aと
の間にガス通路20が接続される。ガス通路20の周囲
には保温用発熱体22が取り付番)られる。[Actual Example 1] FIG. 1 is a conceptual diagram showing an example of a processing apparatus used for carrying out the method of the present invention. This processing equipment has a processing bag: ηl
O, and a plurality of cooling collection devices 12a connected thereto,
..., 12n is input. The heat treatment equipment IO is
Consisting of a heating container 14, a heating element 16, etc., a processing gas supply port 18 is provided at the top, and a cooling collection device! A gas passage 20 is connected between the gas passage 2a and the gas passage 2a. A heat-retaining heating element 22 is attached around the gas passage 20.
加熱容器14は、加熱処理温度にもよるが、例えばタン
グステン等の耐熱性金属材ギ」やアルミナ、高クロム耐
火煉瓦等のセラミックス材寥4で製作される。加熱方法
は、同図に示すように発熱体16に通電することによる
外部加熱の他、高周波加熱、マイクロ波加熱、高放射性
廃棄物への直接通電加熱等の方法も使用できる。また高
放射性廃棄物の崩壊熱による加熱を有効に利用すること
も重要である。The heating container 14 is made of, for example, a heat-resistant metal material such as tungsten, or a ceramic material 4 such as alumina or high-chromium refractory brick, depending on the heat treatment temperature. As a heating method, in addition to external heating by energizing the heating element 16 as shown in the figure, methods such as high frequency heating, microwave heating, and direct energization heating of highly radioactive waste can also be used. It is also important to effectively utilize the heating generated by the decay heat of highly radioactive waste.
加熱容器14の内部に処理すべき高放射性廃棄物24を
入れ加熱を行う、この高放射性廃棄物24は、例えば使
用済核燃料の再処理工程から生じる硝酸溶液を加熱し水
分や硝酸を蒸発さセて得た仮焼体である。勿論、硝酸溶
液の状態からi、I k?的に処理を行うこともできる
。この仮焼体を500 cから3000℃程度まで、よ
り好ましくは1ooo〜2500℃程度まで加熱する。Highly radioactive waste 24 to be treated is placed inside the heating container 14 and heated.This highly radioactive waste 24 is heated, for example, by heating a nitric acid solution generated from the reprocessing process of spent nuclear fuel to evaporate moisture and nitric acid. This is the calcined body obtained by Of course, from the state of the nitric acid solution, i, I k? It is also possible to perform processing manually. This calcined body is heated to about 500°C to 3000°C, more preferably about 100°C to 2500°C.
加熱によって、仮焼体に含まれている元素はそれぞれの
化学形態に応じた昇華点あるいは沸点において気化し、
ガス通路20を通って冷却捕集装置12a、・・、12
nに送られる。By heating, the elements contained in the calcined body are vaporized at the sublimation point or boiling point depending on their chemical form,
The cooling collection devices 12a, . . . , 12 pass through the gas passage 20.
Sent to n.
二の気化した元素は、それらの化学形態での昇華点又は
沸点に対応した温度に制御されている各冷却捕集装置1
2a5・・・、12nで個別に冷却捕集される。The two vaporized elements are stored in each cooling collection device 1 whose temperature is controlled to correspond to the sublimation point or boiling point of their chemical forms.
2a5..., 12n are individually cooled and collected.
加熱工程は常圧中において行ってもよいが、減圧中で行
うと昇華又は沸騰する温度が低下するためより低い温度
で処理することができ、エネルギー効率的にも望ましい
。The heating step may be performed under normal pressure, but when performed under reduced pressure, the sublimation or boiling temperature is lowered, so the process can be performed at a lower temperature, which is also desirable in terms of energy efficiency.
実際には第1段階として酸化物の化学形態で昇華又は沸
騰する元素を常圧もしくは減圧下で加熱処理して分に1
シ、次いで第2段階として水素ガス、炭素又は一酸化炭
素等の還元処理剤を導入しつつ加熱し、高放射性物質を
還元して金属の形態で沸騰又は昇華する元素を分離する
。In fact, in the first step, elements that sublimate or boil in the chemical form of oxides are heat-treated under normal pressure or reduced pressure.
Next, in the second step, heating is performed while introducing a reducing treatment agent such as hydrogen gas, carbon, or carbon monoxide to reduce highly radioactive substances and separate elements that boil or sublimate in the form of metals.
そして最終的に加熱容器14内の残渣を回収する。加熱
容器14からの残渣熔融物25のIJ)出方法としては
、第2図に示すようなボトムフロー式でもよいし、第3
図に示すようなオーバフロ一方式でもよい。何れにして
もこのような形で固化体容器26に残渣溶融物25を排
出し、そのまま冷却することで高減容同化体が得られる
。Finally, the residue inside the heating container 14 is recovered. The method for discharging the residual melt 25 from the heating container 14 may be a bottom flow method as shown in FIG.
An overflow type as shown in the figure may be used. In any case, a highly reduced volume assimilate can be obtained by discharging the residual melt 25 into the solidified material container 26 in this manner and cooling it as it is.
(実験例1)
放射性核種を安定元素で模擬した高放射性廃棄物の模擬
硝酸溶液を蒸発処理して仮焼体を作成した。次いでその
仮焼体を1.000 ℃でI(2He(1:4)の混合
ガス気流中で4時間高温加熱処理した。この間、冷却?
1集部にはTeCd、Se、Cs、Naが析出し捕集で
きた。(Experimental Example 1) A calcined body was created by evaporating a simulated nitric acid solution of highly radioactive waste in which radionuclides were simulated with stable elements. The calcined body was then heat-treated at a high temperature of 1.000°C for 4 hours in a mixed gas flow of I(2He (1:4). During this time, it was cooled?
TeCd, Se, Cs, and Na were precipitated and collected in the first collecting part.
冷却捕集部の各元素に刻する温度は、Teが200〜6
00℃、Cdが200〜300℃、Seが約600℃、
Csが900〜1000℃、Naが6 Q O〜+ 0
00 ’cであった。The temperature applied to each element in the cooling collection section is 200 to 6 for Te.
00℃, Cd 200-300℃, Se about 600℃,
Cs is 900-1000℃, Na is 6 Q O ~ + 0
It was 00'c.
(実験例2)
に記実験例1で高温加熱還元処理した後の仮焼体を、8
50℃〜1050℃で真空中で処理した。冷却捕集部に
はPd及びRuが析出したことが111認された。(Experimental Example 2) The calcined body after the high temperature heating reduction treatment in Experimental Example 1 was
Processed in vacuum at 50°C to 1050°C. It was found that Pd and Ru were precipitated in the cooling collection section.
1発明の効果]
本発明は上記のように高放射性廃棄物を高温で加熱処理
又は加熱還元処理することにより一部の含有元素を分離
捕集する方法であるから、従来提案された各方法に比べ
て処理工程が単純であり、再処理工程や固化工程で新た
に試薬あるいはイオン交換体等を付加せずに済むし、ま
たtili 果される元素は酸化物や金属の固体であり
、放Q1 &i iとしての利用、有用金属としてのf
ll用、史には核種変換による消滅処理等に複雑な二次
処理をすることなしに供し得る。1. Effects of the Invention] As described above, the present invention is a method of separating and collecting some of the contained elements by subjecting highly radioactive waste to heat treatment or heat reduction treatment at high temperatures. Compared to this, the treatment process is simple, and there is no need to add new reagents or ion exchangers during the reprocessing or solidification process. &i Use as i, f as a useful metal
For example, it can be used without complex secondary processing such as annihilation processing due to nuclide transmutation.
また本発明方法により得られる固化体は、核分裂生成物
、アクチニド以外の添加物を殆ど含まず、貯蔵や処分に
おいて占有体積が従来の固化体に比し極めて・j′1さ
くなりコストを大幅に低減し得る。またこの固化体は中
性子照射等による核種変換の照射体としても、体積が小
さく照射効率が高い極めて良好なものとなる。In addition, the solidified material obtained by the method of the present invention contains almost no additives other than fission products and actinides, and occupies an extremely small volume during storage and disposal compared to conventional solidified material, significantly reducing costs. can be reduced. Moreover, this solidified body is very suitable as an irradiation body for nuclide conversion by neutron irradiation, etc. due to its small volume and high irradiation efficiency.
第1図は本発明方法の実施に好適な装置の一例を示す概
念図、第2図はボトムフロ一方式による残渣熔融物の排
出方法を示す説明図、第3図はオーバフロ一方式による
残渣溶融物のiJト出方法を示す説明図である。
10・・・加熱処理装置、12a、・・・、12n・・
・冷却捕集装置、14・・・加熱容器、16・・・発熱
体、20・・・ガス通路、22・・・保温用発熱体、2
4・・・高放射性廃棄物。Fig. 1 is a conceptual diagram showing an example of an apparatus suitable for carrying out the method of the present invention, Fig. 2 is an explanatory diagram showing a method for discharging residual melt using a bottom flow type, and Fig. 3 is an explanatory diagram showing a method for discharging residual melt using a single overflow type. FIG. 2 is an explanatory diagram showing an iJ output method. 10... Heat treatment device, 12a,..., 12n...
- Cooling collection device, 14... Heating container, 16... Heating element, 20... Gas passage, 22... Heating element for heat retention, 2
4...Highly radioactive waste.
Claims (1)
素を気化させて分離し、冷却捕集することを特徴とする
高放射性廃棄物の処理方法。 2、高放射性廃棄物を高温で加熱還元処理し、一部の含
有元素を気化させて分離し、冷却捕集することを特徴と
する高放射性廃棄物の処理方法 3、高放射性廃棄物を高温で加熱処理し、一部の含有元
素を気化させて分離し、それを冷却捕集し、次いで残存
物を高温で加熱還元処理し、一部の含有元素を気化させ
て分離し、それを冷却捕集し、残渣を固化体として回収
することを特徴とする高放射性廃棄物の処理方法。 4、還元処理を水素、炭素又は一酸化炭素を用いて行う
請求項2又は3記載の処理方法。[Claims] 1. A method for processing highly radioactive waste, which comprises heating the highly radioactive waste at a high temperature, vaporizing and separating some of the contained elements, and cooling and collecting the waste. 2. A method for processing highly radioactive waste characterized by subjecting highly radioactive waste to heat reduction treatment at high temperatures, vaporizing and separating some of the contained elements, and cooling and collecting the waste. 3. heat treatment to vaporize and separate some of the contained elements, cool and collect them, then heat and reduce the residue at high temperatures, vaporize and separate some of the contained elements, and cool it. A method for processing highly radioactive waste, characterized by collecting the waste and recovering the residue as a solidified substance. 4. The treatment method according to claim 2 or 3, wherein the reduction treatment is performed using hydrogen, carbon, or carbon monoxide.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019224A JP2633000B2 (en) | 1989-01-28 | 1989-01-28 | How to treat highly radioactive waste |
| AU47980/90A AU628468B2 (en) | 1989-01-28 | 1990-01-16 | Method of treatment of high-level radioactive waste |
| FR9000782A FR2642565B1 (en) | 1989-01-28 | 1990-01-24 | PROCESS FOR TREATING HIGHLY RADIOACTIVE WASTE |
| GB9001722A GB2227599B (en) | 1989-01-28 | 1990-01-25 | Method of treatment of high-level radioactive waste |
| DE19904002316 DE4002316C2 (en) | 1989-01-28 | 1990-01-26 | Process for treating a high level radioactive waste |
| US07/789,528 US5185104A (en) | 1989-01-28 | 1991-11-08 | Method of treatment of high-level radioactive waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019224A JP2633000B2 (en) | 1989-01-28 | 1989-01-28 | How to treat highly radioactive waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02201199A true JPH02201199A (en) | 1990-08-09 |
| JP2633000B2 JP2633000B2 (en) | 1997-07-23 |
Family
ID=11993400
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1019224A Expired - Lifetime JP2633000B2 (en) | 1989-01-28 | 1989-01-28 | How to treat highly radioactive waste |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JP2633000B2 (en) |
| AU (1) | AU628468B2 (en) |
| DE (1) | DE4002316C2 (en) |
| FR (1) | FR2642565B1 (en) |
| GB (1) | GB2227599B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005201765A (en) * | 2004-01-15 | 2005-07-28 | Central Res Inst Of Electric Power Ind | Method for separating nuclides from solid fission product content |
| JP2013019734A (en) * | 2011-07-11 | 2013-01-31 | Taiheiyo Cement Corp | Processing system and processing method for contaminated soil |
| JP2013164410A (en) * | 2012-01-13 | 2013-08-22 | Nippon Steel & Sumitomo Metal | Method for purifying radioactive contaminant |
| JP2016153809A (en) * | 2016-05-02 | 2016-08-25 | 株式会社クボタ | Radioactive cesium separation/concentration method and radioactive cesium separation/concentration apparatus |
| WO2017203567A1 (en) * | 2016-05-23 | 2017-11-30 | 株式会社日立製作所 | Radionuclide separation method and radionuclide separation device |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| MY109384A (en) * | 1991-04-15 | 1997-01-31 | Wimmera Ind Minerals Pty Ltd | Removal of radioactivity from zircon. |
| CN104137189B (en) * | 2011-10-21 | 2017-07-25 | 法国电力公司 | Thermal Purification of Graphite Using Reducing Gas |
| ITCO20130066A1 (en) * | 2013-12-16 | 2015-06-17 | Wow Technology S P A | METHOD TO TREAT AN AQUEOUS SOLUTION / DISPERSION CONTAINING AT LEAST A RADIOACTIVE SUBSTANCE AND PLANTS THAT REALIZE IT |
| CN105895183B (en) * | 2016-04-21 | 2018-01-05 | 中广核研究院有限公司 | Carbon containing 14 waste gas processing method and system |
| DE102018102510B3 (en) * | 2018-02-05 | 2019-06-27 | Kerntechnische Entsorgung Karlsruhe GmbH | Process and apparatus for separating cesium and technetium from radioactive mixtures |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5093865A (en) * | 1973-03-29 | 1975-07-26 | ||
| JPS6056300A (en) * | 1983-09-08 | 1985-04-01 | 日本原子力研究所 | Method of treating waste containing radioactive nuclide |
| JPS63176440A (en) * | 1987-01-16 | 1988-07-20 | Mitsubishi Kasei Corp | heating furnace |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB817861A (en) * | 1953-04-21 | 1959-08-06 | Atomic Energy Authority Uk | Separation of fission products from irradiated uranium |
| BE629323A (en) * | 1962-03-08 | 1900-01-01 | ||
| CS167749B1 (en) * | 1974-03-25 | 1976-05-28 | Bohuslav Cech | Method of uranium,plutonium and their compounds gaining |
| DE2657265C2 (en) * | 1976-12-17 | 1984-09-20 | Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe | Process for the solidification of radioactive waste liquids from the reprocessing of nuclear fuel and / or breeding material in a matrix made of borosilicate glass |
| JPS58191998A (en) * | 1982-05-06 | 1983-11-09 | 動力炉・核燃料開発事業団 | Cyclic tank type microwave heating device |
| PH22647A (en) * | 1984-01-16 | 1988-10-28 | Westinghouse Electric Corp | Immobilization of sodium sulfate radwaste |
| JPS62235218A (en) * | 1986-04-04 | 1987-10-15 | Unitika Ltd | Method for separating and recovering uranium and hydrofluoric acid |
| DE3616391A1 (en) * | 1986-05-15 | 1987-11-19 | Kernforschungsz Karlsruhe | METHOD FOR THE FINE CLEANING OF SPLIT MOLYBDA |
| JPH0648315B2 (en) * | 1987-09-16 | 1994-06-22 | 動力炉・核燃料開発事業団 | Thermal decomposition treatment equipment for radioactive waste |
-
1989
- 1989-01-28 JP JP1019224A patent/JP2633000B2/en not_active Expired - Lifetime
-
1990
- 1990-01-16 AU AU47980/90A patent/AU628468B2/en not_active Ceased
- 1990-01-24 FR FR9000782A patent/FR2642565B1/en not_active Expired - Fee Related
- 1990-01-25 GB GB9001722A patent/GB2227599B/en not_active Expired - Fee Related
- 1990-01-26 DE DE19904002316 patent/DE4002316C2/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5093865A (en) * | 1973-03-29 | 1975-07-26 | ||
| JPS6056300A (en) * | 1983-09-08 | 1985-04-01 | 日本原子力研究所 | Method of treating waste containing radioactive nuclide |
| JPS63176440A (en) * | 1987-01-16 | 1988-07-20 | Mitsubishi Kasei Corp | heating furnace |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005201765A (en) * | 2004-01-15 | 2005-07-28 | Central Res Inst Of Electric Power Ind | Method for separating nuclides from solid fission product content |
| JP2013019734A (en) * | 2011-07-11 | 2013-01-31 | Taiheiyo Cement Corp | Processing system and processing method for contaminated soil |
| JP2013164410A (en) * | 2012-01-13 | 2013-08-22 | Nippon Steel & Sumitomo Metal | Method for purifying radioactive contaminant |
| JP2016153809A (en) * | 2016-05-02 | 2016-08-25 | 株式会社クボタ | Radioactive cesium separation/concentration method and radioactive cesium separation/concentration apparatus |
| WO2017203567A1 (en) * | 2016-05-23 | 2017-11-30 | 株式会社日立製作所 | Radionuclide separation method and radionuclide separation device |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2227599B (en) | 1992-12-23 |
| GB9001722D0 (en) | 1990-03-28 |
| AU628468B2 (en) | 1992-09-17 |
| DE4002316A1 (en) | 1990-08-02 |
| FR2642565A1 (en) | 1990-08-03 |
| DE4002316C2 (en) | 1998-04-09 |
| GB2227599A (en) | 1990-08-01 |
| JP2633000B2 (en) | 1997-07-23 |
| AU4798090A (en) | 1990-08-02 |
| FR2642565B1 (en) | 1994-08-05 |
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