JPS58194742A - Denitration of uranium - Google Patents

Denitration of uranium

Info

Publication number
JPS58194742A
JPS58194742A JP57073361A JP7336182A JPS58194742A JP S58194742 A JPS58194742 A JP S58194742A JP 57073361 A JP57073361 A JP 57073361A JP 7336182 A JP7336182 A JP 7336182A JP S58194742 A JPS58194742 A JP S58194742A
Authority
JP
Japan
Prior art keywords
powder
powders
uranium
fluidized bed
bed
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
JP57073361A
Other languages
Japanese (ja)
Inventor
Masami Odajima
小田島 正見
Tetsuo Morisue
森末 哲夫
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.)
Toshiba Corp
Original Assignee
Toshiba Corp
Tokyo Shibaura Electric Co 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 Toshiba Corp, Tokyo Shibaura Electric Co Ltd filed Critical Toshiba Corp
Priority to JP57073361A priority Critical patent/JPS58194742A/en
Publication of JPS58194742A publication Critical patent/JPS58194742A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Inorganic Compounds Of Heavy Metals (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:Powders of UO2 and/or U3O8 are fed into the fluidized bed of UO3, uranium nitrate is introduced into the bed and the denitration is effected by heating with microwaves, thus conducting denitration without external heaters. CONSTITUTION:UO3 powders, UO2 and/or U3O8 powders are introduced into the fluidized bed 2 and air is fed to make a fluidized state, then uranyl nitrate solution is sprayed from nozzle 4. Microwaves are applied and the powders of UO2 or U3O8 generate heat, because of their large dielectric loss, to gasify the water and nitrogen oxides in the solution and the gases are removed from the exhaust gas treater 5, after UO3, UO2 or U3O8 powders accompanying the gases are separated. In the meantime, the dehydrated and denitrated uranyl nitrate solution is converted into a UO3 powder and the powder is recovered into the recovering tank 9, as it is mixed with UO2 or U3O8 powders. Further, UO3 is converted into U3O8 and UO2 with hydrogen in reductive calciner and UO2 is collected in the vessel 12. A part of the product is contained in the powder feeder 14 for reuse.

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は被処!物を流動床鴫二共給してマイクロ波md
i二より反応を生じさせて被処ム物をm4するよう、に
したウランの脱硝処理方法6二関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is a subject! Microwave md by co-feeding materials in a fluidized bed
This invention relates to a method for denitrifying uranium in which a reaction is caused to reduce the amount of material to be treated to m4.

〔発明の技術的背景〕[Technical background of the invention]

一*1ニー加熱流励床反応装置は、反応塔内(二分奴板
を設け、−分散板上(二流励床を形成させ、このIIL
IIB床内(二被石場吻を導入し、この被処理物を加熱
するものでわる。
1*1 Knee-heated flow excited bed reactor is constructed by forming a double-flow excited bed inside the reaction tower (with a bipartite plate, and above the dispersion plate).
In the IIB bed (introduces two stone holes and heats the material to be treated).

この加熱手段(二は分赦板の下ロレから熱風を圧送する
手段が採られている。
This heating means (second) is a means of pumping hot air from the lower part of the release plate.

含有水分が憂く工樵全俸としてエンタルピ律速なプロセ
スとしてオU用させる一合(二おいては、必菅とするI
I&菫で49ことは技術的もしくは経済的(二燕壇がわ
ル、別の7JIl熱手段を−しる必要がめる。
The first step is to use OU as an enthalpy rate-determining process for all the woodworkers who are worried about the moisture content (in the second case, it is necessary to use I).
49 in I & Sumire, there is a technical or economic need to find another means of heating.

−かかるエンタルピ律速なプロセスの一つとして、使用
績値燃料を再処理する工程の一部分をなす脱硝反&ムエ
掘がある。
- One such enthalpy-limited process is denitrification and mue mining, which forms part of the process of reprocessing historical fuel.

この工程は銅酸クラニル原液を熱分解して水分およびN
O,ガスを放出し、酸化ウラン(二変供するものでTo
l)、約2000 K cat/# U g Kの熱意
が請求される。
This process involves thermally decomposing the cranyl cuprate stock solution to remove moisture and N.
O, gas is released, and uranium oxide (to
l), an enthusiasm of approximately 2000 K cat/# U g K is charged.

このような賛求砿二対して、便乗この樵脱硝反応工程に
用いられる加熱流−床反応装置としては、W&蝋の外鐘
C二抵抗式ヒーター等を設けた外熱方式によシ加熱して
いる。
In response to such support, the heated flow-bed reactor used in the denitrification reaction process is heated by an external heating method equipped with a double-resistance heater, etc. ing.

〔背景技術の問題点〕[Problems with background technology]

この外熱方式(二は、所要の熱意の供給が容易(二かつ
効果的C2行なうことができない問題点が必る。
This external heat method (2) is easy to supply the required heat (2) and requires problems that prevent C2 from being carried out effectively.

即ち、かかる方式(二よると伝M4面積4二限就がある
ため、所要の隔置を供耐する手段を適i選屋しなければ
ならず、0に処理−を増大するため感=装−〇スケール
アップを針る場合にその一定が問題となる。
In other words, since such a method (according to 2) has a limited area of M4 of 42, it is necessary to appropriately select a means to provide the required spacing, and in order to increase the processing capacity to 0, −〇When aiming to scale up, consistency becomes a problem.

一方、必Aな熱jtを確保するため一二訛−床師位の装
置−温を脚くする場合c二は、装置外部への放熱量の増
−大4:1−tPう熱損失が増加することとなる。
On the other hand, in order to secure the necessary amount of heat, the temperature of the device at the level of the 12th grade is lowered. This will result in an increase.

史4:装を壁温を高くすると生成UOs粉末の粒径コン
トロールが困−となシ、がっ流動床の一時的な訛!II
b阻外等に伴う伝熱不良(二よシ流動床の凝集等が生じ
、装置の運転を不能(二する重大なトラブルが発生する
恐れが増大する。
History 4: When the wall temperature of the bed is raised, it becomes difficult to control the particle size of the UOs powder produced, which is a temporary effect of the fluidized bed! II
There is an increased risk of heat transfer failure (such as agglomeration of the fluidized bed, etc.) due to external interference, making it impossible to operate the equipment (2) and other serious troubles.

このようなことから、抵抗式ヒーター等の加熱手段を・
塔内4二設けた内帥加舶方式とすることも考えられるが
、被処理物が放射性切^を首肩するた一1j% ”K、
v)履射性物質O外婦洩れを鋳圧する必要がある。また
ヒーターの保守、交換等ζ;構造上の問題が生じ、かつ
特に一般O円筒臘流動床では粒子のI51動化状−を良
好(ニー持するため6二、内部ヒーターの寸法シニは1
!Kl限を受け、伝熱面積の増大効果は限定される。
For this reason, heating means such as resistance heaters are
It is possible to use an internal control system with 42 units installed inside the tower, but since the material to be treated is exposed to radioactive material,
v) It is necessary to pressurize the leakage of ejectable material O. In addition, maintenance and replacement of the heater, etc., may cause structural problems, and in particular, in a general O cylindrical fluidized bed, the particle I51 mobilization state is good (62 to maintain the knee, and the internal heater size is 1
! Due to the Kl limit, the effect of increasing the heat transfer area is limited.

〔発明の目的〕[Purpose of the invention]

本発明は以上の欠点な除去するため艦=なされたもので
、R#床内の加熱効率を増、太し、間接加熱源として使
用している外−ヒーター等を不用とし、しかも保守点検
が容易となるよう砿二したの脱硝処理方法を提供するこ
とC:ある。
The present invention has been made to eliminate the above drawbacks, and increases and thickens the heating efficiency in the R# floor, eliminates the need for external heaters used as indirect heating sources, and requires less maintenance and inspection. C: Yes, to provide a method for easily denitrifying carbon dioxide.

〔尭−の概要〕[Summary]

上記目的を達成するため本発明は二酸化ウラン流動床内
4二硝酸つ2ニルを導入し、前記硝酸ウラニルを加熱脱
硝するマイクロ波加熱aIIIIIl床りツン脱硝処琥
方法(二おいて、前記流動床内1ニニ畝化ウランまたは
入玉酸化ウランもしくはこれらの混合   “″′粉末
を混入して、IItI紀硝威ウラニルを加熱脱硝するこ
とを特徴とするマイクロ誠加熱fi動床つフン腕−処堀
方法である。
In order to achieve the above object, the present invention introduces uranyl nitrate into a uranium dioxide fluidized bed and heats and denitrates the uranyl nitrate. A micro-serial heating system characterized by heating and denitrifying IItI uranyl by mixing uranium oxide, uranium oxide, or a mixture of these powders. It's a method.

〔始−〇実施例」 以下、図面1に参照しながら本発明(2係るマイクロ波
加熱vL鯛床(二よるウランの脱硝処理方法の一拠彪例
な便用≠核燃料何九理(二2ける脱硝反応工Ii!4=
用いた例で説明する。
[Start-〇Embodiment] Hereinafter, with reference to Drawing 1, the present invention (microwave heating vL sea bream bed according to 2. Reaction Engineering Ii!4=
This will be explained using an example.

図面4二おいて、マイクロ彼発振器1から込られたマイ
クロ波は導阪管形a勤床2丙t〃口熱する。
In FIG. 42, the microwave input from the microwave oscillator 1 heats the conductor pipe type A and the floor.

訛IIt1床2(=は給歇装置3から送られた硝はウラ
ニル#献を!!化する噴−ノズル4と上昇する上気(二
同伴する*#末を排ガス処理装置5(=込る排気ライン
6が設けられている。
Accent IIt1 bed 2 (= is the nitrate sent from the supply device 3 that converts into uranyl #!! - the injection nozzle 4 and the rising upper air (2 entrains the *# end to the exhaust gas treatment device 5 (= includes) An exhaust line 6 is provided.

′また、流動床2の下端≦二は分散値15と給気装置7
から送られた空′At内婦4二供給する給気ライン8及
び2歳化ウランまたは入玉賊化ウランもしくはこれらの
混合切粉末と脱硝生成物の混合粉末を1合粉末回収偵置
94;耕出させる排出2イン10が設けられている・。
'Also, if the lower end of the fluidized bed 2≦2, the dispersion value 15 and the air supply device 7
An air supply line 8 that supplies air 42 from the air supply line 8 and a mixed powder of 2-year-old uranium or impregnated uranium or a mixed powder of these and a denitrification product is collected and recovered 94; A 2-in-10 plowing discharge is provided.

一方混合粉末は、焙廃迩元装置111mより二酸化ウラ
ンは入玉酸化92ン(2変IAされ、さら(ユニ酸化ウ
ラン(:;41元されて生成物格納容器12(二回収さ
れる。生成物の一1Ilは粉末供給装置13を通って、
粉末供給装置14(二送られ再使用される。
On the other hand, from the mixed powder, uranium dioxide is transferred from the waste disposal equipment 111m to 92 ton oxidation (2 conversion IA), and further (unionized uranium oxide (:; 41 ton) is converted to product storage vessel 12 (2 conversion. The material 1Il passes through the powder supply device 13,
Powder feeding device 14 (second feed and reuse).

なお図中符号16.17はパルプを示している。Note that numerals 16 and 17 in the figure indicate pulp.

以上の様なAl11において、三−化り2ン扮末と二酸
化ウラン゛または入玉酸化ウランもしくはこれらの混合
粉末をvt励尿2内(二所定童入れ、艙気誠d7から送
られたを気を一定i給気し、1合粉末なは鯛させた状悪
で硝酸ソラニル浴f&を噴霧ノズル4N二より4化して
供給する。
In the Al11 as described above, the tri-condensed powder and uranium dioxide or uranium oxide or a mixed powder thereof are placed in the vt excimer 2 (in the designated nursery case, the one sent from the Air is supplied at a constant rate, and the solanyl nitrate bath f& is supplied from a 4N spray nozzle to a 4N spray nozzle.

一方マイクロ波は、導d’jF形fE、−床2内(二供
給されているため、−4体損失(atanJ)が大きい
二酸化ウランまたは入玉は化ウランの粉体は、UO3粉
体が技部しえなかったエネルギーをも技部して発熱し、
硝酸つ2ニル溶液中にtまれる水分及び意素威化切は水
蒸気及びNO,刀スとなる。
On the other hand, the microwave is guided d'jF type fE, - in the bed 2 (2), so the -4 body loss (atanJ) is large for uranium dioxide or injected uranium oxide powder, and UO3 powder is Energy that could not be generated by the technical department is also generated by the technical department,
The water and water added to the nitric acid solution become water vapor, NO, and gas.

この水蒸気及びNO,を含Mする排ガスは上昇するが、
この排ガスはUOsOs米粉末二ば化ウランlたは入玉
酸化ウランの微粉末を同伴するため、この微粉末を排ガ
ス36虐装*t5で除六した債、大気へ放出される。
This exhaust gas containing water vapor and NO rises,
Since this exhaust gas is accompanied by fine powder of UOsO rice powder uranium dibanide or injected uranium oxide, this fine powder is removed by exhaust gas 36*t5 and released into the atmosphere.

一方h8品脱水及び脱硝した、硝1ウラニル溶液は、U
 Os粉末となシ、二酸化ウランまたは入玉ば化ウラン
の粉末と混合しながら排出ライン10を通りて晶合粉禾
@収装置9(二回収される。
On the other hand, the H8 product dehydrated and denitrified nitrate-1 uranyl solution is U
The Os powder is mixed with uranium dioxide or injected uranium oxide powder and passed through a discharge line 10 to be collected by a crystallization device 9 (two collection devices).

さら4二回収した一合扮不は、焙7A4元1により三酸
化I72ンはまr入玉酸1ヒウラン(ユ、さらζ二水A
ガス雰囲気中で二酸化ウラン(二転換される。
In addition, 42 recovered Ichigobanfu were mixed with I72 trioxide by roasting 7A 4 parts 1 and 1 hiuran (Yu, Sara ζ dihydroA).
Uranium dioxide (diconverted) in a gas atmosphere.

−洟生成物は生成種格納容器12に回収される。また妖
侯生成−の一錫は掻送J装置13を通って粉末供IIi
!1装置14に収納され、再に用される。
- The product is collected in the product storage vessel 12. In addition, the tin produced by Youhou passes through the scraper J device 13 and is supplied with powder IIi.
! 1 device 14 and used again.

上m1−Aゐ例は特に便用揖該燃料の丹凪臘工程の−4
をなす脱硝反応工@(ニジいて多産の被処理物(IJ1
1#クラニル痔液)を処4するのに適する。
The above m1-A example is especially for the -4 of the tangent process of the fuel for convenience.
Denitrification reaction process (IJ1)
Suitable for treating 1# Cranil hemorrhoid fluid).

即ちかかる一逃壇物は、臨界安全的問題から流動床の塔
径または、幅に巾U約をうけるが、図≦;示す411:
A−A’矢祝で示したに一床の1−の寸法を、100〜
150 mにすれば臨界安全的問題はない。
In other words, the width of such a single bed is limited to the column diameter or width of the fluidized bed due to criticality safety issues, but the width U is limited to the column diameter or width of the fluidized bed.
The dimension of 1- of one bed shown by A-A' arrow is 100~
If the distance is set to 150 m, there will be no criticality safety issue.

〔発明の効果〕〔Effect of the invention〕

上述した悼毫二本開明の反応処]刀法6二おいては、4
波管形流動床内(:混入した二酸化クランまた杜入玉誠
化り2ン自身が、マイクロ波を1収して角熱し間接的な
FA源となるもので、従来マイクg波エネルギーの50
−を損失していたが、ニー化ウランまたは入玉誠化ウラ
ン粉末を混入すること4二よシ、エネルギー損失が減少
し、加熱効率が大きくなる。
In the above-mentioned reaction of Sogo Nihon Kaimei] Toho 62, 4
Inside the corrugated tube-shaped fluidized bed (: the mixed carbon dioxide and the carbon dioxide contained in the dui-in tama-seikan itself absorbs microwaves and heats them up, becoming an indirect FA source.
However, by mixing uranium nitride or cemented uranium powder, the energy loss will be reduced and the heating efficiency will be increased.

したがって、流動床内(二哄霧供給される溶液あるいは
、fi勧床(二分散又はj6f、する水分を容易櫨二加
熱することができる。
Therefore, it is possible to easily heat the solution in the fluidized bed or the water that is dispersed in the fluidized bed.

本発明の効果′lk:Jjjl約すれば下記のとお)で
ある。
The effects of the present invention are summarized as follows.

(1)■二酸化ウランまたはへ五酸化りツy自身がマイ
クロ波を吸収し発熱するため、flLi#床内O加床内
重加熱効率な)、被処理物を短時間嬬二魁塩することが
できる。
(1) Since uranium dioxide or pentoxide itself absorbs microwaves and generates heat, the material to be treated can be salted for a short time. I can do it.

(2)従来間接熱1として用いていた外部ヒーター等が
不用となるため鋏11Lの保守点検が容易1二なる。
(2) Maintenance and inspection of the scissors 11L becomes easier because an external heater, etc., which was conventionally used as indirect heat 1, is no longer required.

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

図面は本発明方法を一―するためのマイク−波加熱流−
床反応装置を、3し公的(二断面で示すブロック図で必
る。 l・・・・・・マイクロ波9?i懺器 2・・・・・・導波・υ形gn、−床 3・・・・・・給液装置 4・・・・・・−霧ノズル 5・・・・・・舟カス処理装置 7・・・・・・給気装置 9・・・・・・混合粉未回収装置 11・・・・・・焙腕越元S&匝 12・・・・・・生取り格納容器 13・・・・・・粉末移送絞は 14・・・・・・粉末供帖装置 15・・・・・・分散板
The drawing shows a microphone wave heating flow for carrying out the method of the present invention.
The bed reactor is 3 public (required in the block diagram shown in two cross sections. l...Microwave 9?i Stainless steel 2... Waveguide/υ type gn, -bed 3...Liquid supply device 4...Mist nozzle 5...Boat waste processing device 7...Air supply device 9...Mixed powder Unrecovered device 11... Roasted arm S and bowl 12... Raw collection storage container 13... Powder transfer diaphragm 14... Powder storage device 15・・・・・・Dispersion plate

Claims (2)

【特許請求の範囲】[Claims] (1)三酸化ウラン流動床内ζ二硝酸つラニル耐献を導
入し、マイクロ波照射4二より該流動床内の硝はクラニ
ル祷?11’加熱して脱硝処埴する万床において、前記
流動床内ζ二二威化つツンまたはへ三戚化ウランもしく
はこれらの一合粉末を1人して前記−一り2ニルを加熱
脱硝することを待砿とするウランの脱硝処理方法。
(1) Introducing ζ dinitrate trioxide in a uranium trioxide fluidized bed, and using microwave irradiation (42), the nitrate in the fluidized bed was exposed to cranyl. 11' In the heating and denitrification process, heat denitrification of the ζ22, uranium chloride, or a combined powder of these in the fluidized bed. A method for denitrification of uranium.
(2)流動床4二は粉末回収tcit1焙虎還元装置、
粉本移送装置および粉末供給装置が設けられていること
を時砿とする*a’を請求範囲第1項記載のウランの脱
硝A壇方伝。
(2) The fluidized bed 42 is a powder recovery tcit1 rotor reduction device,
The uranium denitrification method A Dankaden according to claim 1, where *a' is defined as the provision of a powder transfer device and a powder supply device.
JP57073361A 1982-05-04 1982-05-04 Denitration of uranium Pending JPS58194742A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57073361A JPS58194742A (en) 1982-05-04 1982-05-04 Denitration of uranium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57073361A JPS58194742A (en) 1982-05-04 1982-05-04 Denitration of uranium

Publications (1)

Publication Number Publication Date
JPS58194742A true JPS58194742A (en) 1983-11-12

Family

ID=13515951

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57073361A Pending JPS58194742A (en) 1982-05-04 1982-05-04 Denitration of uranium

Country Status (1)

Country Link
JP (1) JPS58194742A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0348384A2 (en) * 1988-06-22 1989-12-27 Maschinenfabrik Andritz Actiengesellschaft Process and apparatus for producing metal oxides
US6228337B1 (en) * 1998-12-02 2001-05-08 Cameco Corporation Method for reducing uranium trioxide
JP2011088767A (en) * 2009-10-20 2011-05-06 Japan Atomic Energy Agency Method for producing metal oxide particles using microwave absorption-exothermic effect by product addition
CN107771163A (en) * 2015-06-12 2018-03-06 阿雷瓦核废料回收公司 The product that thermal denitration apparatus and method, the application of the equipment and this method obtain
CN114644359A (en) * 2020-12-18 2022-06-21 中核四0四有限公司 Preparation of UO by using natural gas to carry out uranyl nitrate pyrolysis denitration3Method (2)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0348384A2 (en) * 1988-06-22 1989-12-27 Maschinenfabrik Andritz Actiengesellschaft Process and apparatus for producing metal oxides
US6228337B1 (en) * 1998-12-02 2001-05-08 Cameco Corporation Method for reducing uranium trioxide
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