JP2908584B2 - Radioactive waste melting equipment - Google Patents

Radioactive waste melting equipment

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Publication number
JP2908584B2
JP2908584B2 JP3074364A JP7436491A JP2908584B2 JP 2908584 B2 JP2908584 B2 JP 2908584B2 JP 3074364 A JP3074364 A JP 3074364A JP 7436491 A JP7436491 A JP 7436491A JP 2908584 B2 JP2908584 B2 JP 2908584B2
Authority
JP
Japan
Prior art keywords
waste
abutment
radioactive waste
heating element
conductive ceramic
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
Application number
JP3074364A
Other languages
Japanese (ja)
Other versions
JPH04286999A (en
Inventor
年 上原
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.)
NIPPON GAISHI KK
Original Assignee
NIPPON GAISHI KK
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 NIPPON GAISHI KK filed Critical NIPPON GAISHI KK
Priority to JP3074364A priority Critical patent/JP2908584B2/en
Publication of JPH04286999A publication Critical patent/JPH04286999A/en
Application granted granted Critical
Publication of JP2908584B2 publication Critical patent/JP2908584B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Gasification And Melting Of Waste (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は放射性廃棄物を溶融処理
する装置に関するもので、さらに詳しくは1300℃以上の
高温においても使用可能な溶融処理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 an apparatus for melting and processing radioactive waste, and more particularly to a melting apparatus which can be used at a high temperature of 1300.degree.

【0002】[0002]

【従来の技術】従来原子力発電所等の放射性物質取扱施
設から発生する、放射能によって汚染された廃棄物のう
ち可燃性のものは、一般的には焼却処理され、その焼却
灰はドラム罐等に充填されて施設内の適当な場所に貯蔵
されているのが普通である。しかしながらこれら焼却灰
は、粉粒状であるため、焼却灰を充填したドラム罐を輸
送または貯蔵するにあたっては焼却灰の安定化、減容処
理を施すことが望ましく、その処理法がいろいろ研究さ
れている。最近提案されているこれら放射性廃棄物の処
理法としては、例えば放射性廃棄物又は焼却灰をセメン
トで固化する第1の方法、放射性廃棄物又は焼却灰にア
スファルト、プラスチック等を混合して固化する第2の
方法、放射性廃棄物または焼却灰を高温度で加熱溶融固
化する第3の方法がある。
2. Description of the Related Art Conventionally, combustible waste generated from radioactive material handling facilities such as nuclear power plants is incinerated, and the incinerated ash is discharged from drums, etc. And is stored in a suitable place in the facility. However, since these incinerated ash are in powder form, it is desirable to stabilize and reduce the volume of incinerated ash when transporting or storing drums filled with incinerated ash, and various treatment methods have been studied. . Recently proposed methods of treating these radioactive wastes include, for example, the first method of solidifying radioactive waste or incinerated ash with cement, and the first method of mixing radioactive waste or incinerated ash with asphalt or plastic to solidify it. There is a second method, a third method for heating and solidifying radioactive waste or incinerated ash at a high temperature.

【0003】これら各方法を詳細に検討すると、第1の
方法であるセメント固化法においては、廃棄物または灰
とセメントとを混合して、安定した密度、強度等をもつ
固化体を得るには、灰等とセメントとの重量割合を灰等
を1に対してセメント4以上とする必要があり、このた
め固化体容積が灰等の容積よりも増大し増容となってし
まう不具合があった。また、第2の方法であるアスファ
ルトおよびプラスチック固化法においては、廃棄物また
は焼却灰中の金属片の除去、粉体化等の前処理が必要で
あり、設備が複雑かつ大型となる不具合があった。さら
に、第3の方法である加熱溶融固化法においては、上述
した第1および第2の方法で生じる不具合を有効に除去
できるが、廃棄物または焼却灰を高温度で溶融するため
電磁誘導によって鉄等の金属容器を加熱して高温度を達
成しており、金属容器の材質上の制約から1000〜1200℃
の温度での使用が限界であり、それ以上の高温で溶融す
る廃棄物等の溶融処理ができないという不具合があっ
た。
[0003] When each of these methods is examined in detail, in the cement solidification method, which is the first method, it is necessary to mix waste or ash with cement to obtain a solidified material having a stable density, strength, and the like. It is necessary to make the weight ratio of ash etc. and cement to ash etc. 1 or more to cement 4 or more, so that the volume of the solidified body becomes larger than the volume of ash etc., resulting in an increase in volume. . In addition, the asphalt and plastic solidification method, which is the second method, requires pretreatment such as removal of metal fragments from waste or incinerated ash and pulverization, so that the equipment becomes complicated and large. Was. Furthermore, in the third method, the heat-melt solidification method, the problems caused by the first and second methods described above can be effectively removed. However, since the waste or incinerated ash is melted at a high temperature, the iron is removed by electromagnetic induction. High temperature is achieved by heating metal containers such as
However, there is a problem that the melting treatment of wastes and the like that melt at a higher temperature cannot be performed.

【0004】これに対し本願出願人は先に廃棄物収納容
器を導電性セラミックス発熱体とした装置を提案済みで
あり、この装置によれば、金属容器の材質を導電性セラ
ミック発熱体としたため、1300℃〜1600℃の高温におい
て溶融する廃棄物等の溶融処理を実現することができ
る。
On the other hand, the applicant of the present application has already proposed an apparatus using a waste storage container as a conductive ceramic heating element. According to this apparatus, the metal container is made of a conductive ceramic heating element. It is possible to realize a melting treatment of wastes and the like that melt at a high temperature of 1300 ° C to 1600 ° C.

【0005】[0005]

【発明が解決しようとする課題】しかしながら上記の装
置においては、1300℃〜1600℃の高温は達成できるもの
の、容器自体の発熱量の上限はその大きさ等によって規
定されるため限界があり、したがって溶融処理速度を所
望の速度まで高めることが難しかった( ここで再使用で
きない廃棄物収納容器の大型化や電磁誘導加熱コイルの
高出力化により溶融処理速度を高めることも考えられる
が、その場合コストアップを招き、得策でない) 。また
上記装置においては、前記容器の下面に当接し断熱材等
の非金属より成る支台は、ヒートサイクルによってその
上面が脆くなり、耐久性の低下を招く。
However, in the above-described apparatus, although a high temperature of 1300 ° C. to 1600 ° C. can be achieved, the upper limit of the calorific value of the container itself is limited by its size and the like, so there is a limit. It was difficult to increase the melt processing speed to the desired speed. (It is conceivable to increase the melt processing speed by increasing the size of waste storage containers that cannot be reused and increasing the output of electromagnetic induction heating coils. It is not a good idea to invite up). Further, in the above-described apparatus, the upper surface of the abutment made of a non-metal such as a heat insulating material, which is in contact with the lower surface of the container, becomes brittle due to a heat cycle, and causes a decrease in durability.

【0006】本発明の目的は上述した不具合を解消し
て、高温において放射性廃棄物等を高速度で溶融処理し
て輸送、貯蔵に適した安定な減容固化体にする溶融処理
装置を提供しようとするものである。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems and to provide a melting processing apparatus for melting a radioactive waste or the like at a high speed at a high temperature to obtain a stable reduced volume solidified body suitable for transportation and storage. It is assumed that.

【0007】[0007]

【課題を解決するための手段】本発明の放射性廃棄物の
溶融処理装置は、昇降可能な底蓋によって底部を閉鎖し
得る炉本体と、前記炉本体の側壁の外周部に巻装される
電磁誘導加熱コイルと、前記底蓋上に固設される支台
と、前記支台上に載置され前記電磁誘導加熱コイルによ
って高温に電磁誘導加熱される、導電性セラミック発熱
体より成る廃棄物収納容器と、前記炉本体の上蓋に設け
られる炉内排ガス排出口と、前記廃棄物収納容器中へ放
射性廃棄物を投入する廃棄物供給口とを具えて成り、か
つ前記支台の少なくとも上部を導電性セラミック発熱体
によって構成したことを特徴とするものである。
According to the present invention, there is provided a radioactive waste melting apparatus, comprising: a furnace main body whose bottom can be closed by a vertically movable bottom cover; and an electromagnetic wave wound around an outer peripheral portion of a side wall of the furnace main body. Waste storage comprising an induction heating coil, an abutment fixed on the bottom cover, and a conductive ceramic heating element mounted on the abutment and electromagnetically heated to a high temperature by the electromagnetic induction heating coil. A container, a furnace exhaust gas outlet provided in the upper lid of the furnace body, and a waste supply port for introducing radioactive waste into the waste storage container, and at least an upper part of the abutment is electrically conductive. Characterized by comprising a conductive ceramic heating element.

【0008】[0008]

【作用】本発明においては、廃棄物収納容器の他に、そ
れを載置する支台の上部をも導電性セラミック発熱体に
よって構成しているため、容器および支台の上部が誘導
加熱によって効果的に発熱し、所望の高温度(例えば13
00℃〜1600℃) および所望の熱量が得られ、溶融処理速
度が向上する。また支台は少なくともその上部をC-SiC
系、C-Al2O3 系等の導電性セラミック発熱体としている
ため、耐熱衝撃性に優れ、耐久性(寿命)が向上する。
According to the present invention, in addition to the waste storage container, the upper portion of the abutment on which the waste storage container is mounted is also formed of a conductive ceramic heating element. Heat to a desired high temperature (for example, 13
(00 ° C. to 1600 ° C.) and a desired calorific value, and the melt processing speed is improved. In addition, at least the upper part of the abutment is C-SiC
System, C-Al 2 O 3 system or other conductive ceramic heating element, so it has excellent thermal shock resistance and improved durability (life).

【0009】[0009]

【実施例】以下図面を参照して本発明を詳細に説明す
る。図1は本発明の溶融処理装置の一実施例を示す断面
図である。図1において、基礎に立設した支枠1により
支持された密閉容器状の炉本体2は、非金属材料、例え
ば石英質製の円筒状の側壁3と、これに被着された金属
製の蓋部4とから成る。基礎に立設したガイド5によっ
て昇降自在に案内され図示しないモーター等の駆動装置
により昇降駆動される昇降台6には、炉本体2の底部を
解放自在に閉鎖する底蓋7を固着する。側壁3の外周部
には誘導加熱コイル8を取付ける。この誘導加熱コイル
8はカバー9内に収められ、空冷あるいは水冷などの公
知の冷却方法によって冷却される。一方、炉本体2の側
壁3の内側にはアスベスト、キャスタブル等の断熱材よ
り成る円筒状の断熱壁11を設ける。断熱壁11の上端部に
は孔12をそなえた断熱蓋13が被着され、この断熱蓋13は
炉本体2または支枠1に固定支持されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the drawings. FIG. 1 is a sectional view showing one embodiment of the melt processing apparatus of the present invention. In FIG. 1, a closed vessel-shaped furnace body 2 supported by a support frame 1 erected on a foundation includes a cylindrical side wall 3 made of a non-metallic material, for example, quartz, and a metal-made side wall 3 attached thereto. And a lid 4. A bottom cover 7 for closing the bottom of the furnace main body 2 releasably is fixed to a lift 6 that is guided vertically by a guide 5 erected on a base and is driven up and down by a drive device such as a motor (not shown). An induction heating coil 8 is attached to the outer peripheral portion of the side wall 3. The induction heating coil 8 is accommodated in a cover 9 and cooled by a known cooling method such as air cooling or water cooling. On the other hand, a cylindrical heat insulating wall 11 made of a heat insulating material such as asbestos or castable is provided inside the side wall 3 of the furnace body 2. An insulating cover 13 having a hole 12 is attached to the upper end of the insulating wall 11, and the insulating cover 13 is fixedly supported on the furnace body 2 or the support frame 1.

【0010】また、底蓋7上には、導電性セラミック発
熱体、好ましくは C-SiC系または C-Al2O3系セラミック
スより成る上部14a および、その下面に固着される下部
14b( 断熱材等の非金属) より成る支台14が固設されて
おり、支台14上には上記と同様の導電性セラミック発熱
体より成る廃棄物収納容器15を載置する。容器15は底蓋
7およびこれと一体の支台14と共に昇降駆動され、断熱
壁11内に下方から挿脱自在に構成されている。炉本体2
の上部には排ガス排出口16を設けて、溶融時の排ガス等
を断熱蓋13に設けた孔12を介して外部へ導く構成をとっ
ている。また、炉本体2の蓋部4には、廃棄物収納容器
15内へ放射性廃棄物等を供給する廃棄物供給口17、およ
び必要に応じ容器15中へ供給される廃棄物または焼却灰
中の未燃分を燃焼させるに必要な酸素含有ガスを供給す
る酸素供給管18が設けられ、さらに容器15内の溶融状態
を検知する放射温度計、液面計、モニタTV等の検知装置
19をそれぞれ蓋部4を貫通して取付ける。さらにまた、
装置外部の図示しない窒素供給装置からN2 を装置内部
に導く窒素パージノズル20を断熱壁11等を貫通して設
け、炭素を含有しているため酸化され易い、支台14の上
部14a および容器15の酸化劣化を防止する。なお、支台
の上部14a の酸化劣化防止を一層確実にするため、その
表面にフリット材を塗布してガラス層を形成してもよ
い。
On the bottom cover 7, an upper portion 14a made of a conductive ceramic heating element, preferably a C-SiC or C-Al 2 O 3 type ceramic, and a lower portion fixed to the lower surface thereof are provided.
An abutment 14 made of 14b (a non-metal such as a heat insulating material) is fixed, and a waste storage container 15 made of the same conductive ceramic heating element as described above is placed on the abutment 14. The container 15 is driven up and down together with the bottom cover 7 and the support 14 integral therewith, and is configured to be able to be inserted into and removed from the heat insulating wall 11 from below. Furnace body 2
An exhaust gas outlet 16 is provided in the upper part of the housing, and the exhaust gas and the like at the time of melting are guided to the outside through the hole 12 provided in the heat insulating lid 13. The lid 4 of the furnace body 2 includes a waste storage container.
A waste supply port 17 for supplying radioactive waste and the like to the inside 15, and oxygen for supplying an oxygen-containing gas necessary for burning unburned matters in the waste or incineration ash supplied to the container 15 as necessary. A supply pipe 18 is provided, and a detection device such as a radiation thermometer, a liquid level gauge, and a monitor TV for detecting the molten state in the container 15
19 are attached through the lid 4 respectively. Furthermore,
A nitrogen purge nozzle 20 for guiding N 2 from the nitrogen supply device (not shown) outside the device to the inside of the device is provided through the heat insulating wall 11 and the like, and the upper portion 14a of the support 14 and the container 15 which are easily oxidized because they contain carbon. To prevent oxidative degradation of In order to further prevent oxidation deterioration of the upper portion 14a of the abutment, a frit material may be applied to the surface to form a glass layer.

【0011】上記構成を有する放射性廃棄物の溶融処理
装置21においては、誘導加熱コイル8に通電すると導電
性セラミック発熱体より成る廃棄物収納容器15自体が直
接加熱されるとともに支台14の上部14a も直接加熱され
るため、1300〜1600℃の高温域で廃棄物を溶融処理する
ことができる。その際、容器15および導電性耐火物14a
に用いる導電性セラミック発熱体の材質を例えば C-Al2
O3系セラミックスとした場合、電気比抵抗値は炭素含有
量に応じて5×10 -3(Ω・cm) 〜15×10 -3(Ω・cm) と
なり、容器15の重量を140(kg) 、加熱温度を1400(℃)
、支台の上部14a の重量を 60(kg) 、加熱温度を 1200
(℃) としたとき、容器15の熱容量 (発熱量) は 140(kg) ×0.3(Kcal/kg ℃) ×1400 (℃) =58800(Kcal) となり、支台の上部14a の熱容量 (発熱量) は 60(kg)×0.3(Kcal/Kg ℃) ×1200 (℃) =21600(Kcal) となる。したがって支台の上部14a からは容器15の発熱
量の36%に相当する発熱量を得ることができ、廃棄物の
溶融処理を所望の速度(高速度)で行うために必要な発
熱量を容器15単独では確保できなくても、その不足分を
耐火物14a からの発熱量によって補うことができる。
In the radioactive waste melting apparatus 21 having the above structure, when the induction heating coil 8 is energized, the waste storage container 15 itself made of a conductive ceramic heating element is directly heated and the upper part 14a of the abutment 14 is heated. Is also directly heated, so that the waste can be melted in a high temperature range of 1300 to 1600 ° C. At that time, the container 15 and the conductive refractory 14a
The material of the conductive ceramic heating element for use, for example, C-Al 2
In the case of using O 3 ceramics, the electric resistivity value is 5 × 10 −3 (Ω · cm) to 15 × 10 −3 (Ω · cm) depending on the carbon content, and the weight of the container 15 is 140 (kg). ), Heating temperature 1400 (℃)
The weight of the upper part 14a of the abutment is 60 (kg) and the heating temperature is 1200
(° C), the heat capacity (calorific value) of the container 15 is 140 (kg) × 0.3 (Kcal / kg ° C) × 1400 (° C) = 58800 (Kcal), and the heat capacity (calorific value) of the upper part 14a of the abutment ) Is 60 (kg) × 0.3 (Kcal / Kg ℃) × 1200 (℃) = 21600 (Kcal). Therefore, a calorific value equivalent to 36% of the calorific value of the container 15 can be obtained from the upper part 14a of the abutment, and the calorific value necessary for performing the melting processing of the waste at a desired speed (high speed) can be obtained. Even if it cannot be secured by itself, the shortfall can be compensated for by the calorific value from the refractory 14a.

【0012】なお、容器15内の溶融物が所定の量になっ
たら、炉本体2を自然放冷などで冷却し、溶融物が容器
15内で固化して容器15内に固定化されたら、昇降台6を
降下させ容器15を支台14上から取去って、新たな容器15
を支台14上に載置し、以下上記と同様な工程を繰返すも
のとする。
When the melt in the vessel 15 reaches a predetermined amount, the furnace body 2 is cooled by natural cooling or the like, and
When solidified in the container 15 and fixed in the container 15, the elevator 6 is lowered, the container 15 is removed from the support 14, and a new container 15 is removed.
Is mounted on the abutment 14, and the same steps as described above are repeated.

【0013】本発明は上述した実施例にのみ限定される
ものではなく、幾多の変形、変更が可能である。例え
ば、炉本体2が断熱性に富む場合は断熱壁11および断熱
蓋13を省略してもよい。
The present invention is not limited to the above-described embodiment, but can be variously modified and changed. For example, when the furnace main body 2 is rich in heat insulation, the heat insulation wall 11 and the heat insulation lid 13 may be omitted.

【0014】[0014]

【発明の効果】以上詳細に説明したところから明らかな
ように、本発明の放射性廃棄物の溶融処理装置によれ
ば、廃棄物収納容器およびそれを載置する支台の少なく
とも上部を導電性セラミック発熱体によって構成したた
め、容器および支台の上部が誘導加熱によって効果的に
発熱し、所望の高温度(例えば1300℃〜1600℃) および
所望の熱量が得られ、従来1300℃以上の高温で溶融処理
することが不可能であった放射性廃棄物を高速度で溶融
処理することができる。また支台はその上部を C-SiC
系、C-Al2O3 系等の導電性セラミック発熱体としている
ため、耐熱衝撃性に優れ、耐久性(寿命)が向上する。
As is apparent from the above description, according to the radioactive waste melting apparatus of the present invention, at least the upper part of the waste storage container and the abutment on which the waste storage container is mounted is made of a conductive ceramic. Because of the heating element, the upper part of the container and abutment is effectively heated by induction heating, and a desired high temperature (for example, 1300 ° C to 1600 ° C) and a desired amount of heat can be obtained. Radioactive waste that could not be treated can be melted at a high speed. The abutment has C-SiC on the top.
System, C-Al 2 O 3 system or other conductive ceramic heating element, so it has excellent thermal shock resistance and improved durability (life).

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の放射性廃棄物の溶融処理装置の一実施
例を示す断面図である。
FIG. 1 is a cross-sectional view showing an embodiment of a radioactive waste melting apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

2 炉本体 6 昇降台 7 底蓋 8 誘導加熱コイル 14 支台 14a 支台の上部 14b 支台の下部 15 廃棄物収納容器 17 廃棄物供給口 20 窒素パージノズル 21 溶融処理装置 2 Furnace body 6 Elevator 7 Bottom lid 8 Induction heating coil 14 Abutment 14a Upper abutment 14b Lower abutment 15 Waste container 17 Waste supply port 20 Nitrogen purge nozzle 21 Melting equipment

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F23G 5/00 115 F23G 7/00 J 7/00 103Z 103 B09B 3/00 303K ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification code FI F23G 5/00 115 F23G 7/00 J 7/00 103Z 103 B09B 3/00 303K

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 昇降可能な底蓋によって底部を閉鎖し得
る炉本体と、前記炉本体の側壁の外周部に巻装される電
磁誘導加熱コイルと、前記底蓋上に固設される支台と、
前記支台上に載置され前記電磁誘導加熱コイルによって
高温に電磁誘導加熱される、導電性セラミック発熱体よ
り成る廃棄物収納容器と、前記炉本体の上蓋に設けられ
る炉内排ガス排出口と、前記廃棄物収納容器中へ放射性
廃棄物を投入する廃棄物供給口とを具えて成り、かつ前
記支台の少なくとも上部を導電性セラミック発熱体によ
って構成したことを特徴とする、放射性廃棄物の溶融処
理装置。
1. A furnace body whose bottom can be closed by a bottom cover that can be raised and lowered, an electromagnetic induction heating coil wound around an outer peripheral portion of a side wall of the furnace body, and an abutment fixed on the bottom cover. When,
A waste storage container that is placed on the abutment and is electromagnetically heated to a high temperature by the electromagnetic induction heating coil and that is made of a conductive ceramic heating element, and an in-furnace exhaust gas outlet provided in an upper lid of the furnace body, Melting the radioactive waste, comprising: a waste supply port for charging the radioactive waste into the waste storage container; and at least the upper portion of the abutment is constituted by a conductive ceramic heating element. Processing equipment.
【請求項2】 前記導電性セラミック発熱体は C-SiC系
または C-Al2O3系セラミックスより成ることを特徴とす
る、請求項1記載の放射性廃棄物の溶融処理装置。
2. The radioactive waste melting treatment apparatus according to claim 1, wherein the conductive ceramic heating element is made of a C-SiC-based or C-Al 2 O 3 -based ceramic.
JP3074364A 1991-03-15 1991-03-15 Radioactive waste melting equipment Expired - Fee Related JP2908584B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3074364A JP2908584B2 (en) 1991-03-15 1991-03-15 Radioactive waste melting equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3074364A JP2908584B2 (en) 1991-03-15 1991-03-15 Radioactive waste melting equipment

Publications (2)

Publication Number Publication Date
JPH04286999A JPH04286999A (en) 1992-10-12
JP2908584B2 true JP2908584B2 (en) 1999-06-21

Family

ID=13545027

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3074364A Expired - Fee Related JP2908584B2 (en) 1991-03-15 1991-03-15 Radioactive waste melting equipment

Country Status (1)

Country Link
JP (1) JP2908584B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6515437B2 (en) * 2013-08-06 2019-05-22 宗澤 潤一 Processing method of cesium adsorption slurry
JP6409276B2 (en) * 2014-01-28 2018-10-24 宗澤 潤一 Processing method of cesium adsorption slurry
JP6423194B2 (en) * 2014-07-23 2018-11-14 日立Geニュークリア・エナジー株式会社 Solidification method for radioactive waste

Also Published As

Publication number Publication date
JPH04286999A (en) 1992-10-12

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