JP2013170290A - Molten salt electrolysis apparatus and molten salt electrolysis method - Google Patents

Molten salt electrolysis apparatus and molten salt electrolysis method Download PDF

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JP2013170290A
JP2013170290A JP2012034331A JP2012034331A JP2013170290A JP 2013170290 A JP2013170290 A JP 2013170290A JP 2012034331 A JP2012034331 A JP 2012034331A JP 2012034331 A JP2012034331 A JP 2012034331A JP 2013170290 A JP2013170290 A JP 2013170290A
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molten salt
crucible
electrode
recovery
electrolytic
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JP5787785B2 (en
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Shingo Mazaki
信吾 真崎
Takashi Omori
孝 大森
Hitoshi Nakamura
等 中村
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Toshiba Corp
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Abstract

PROBLEM TO BE SOLVED: To solve the problem that heating for a long time is necessary to evaporate and remove a salt, in a salt removing process in a spent fuel reprocessing step.SOLUTION: A molten salt electrolysis apparatus 20 includes: a crucible 14 for accommodating a molten salt 2; a heating means 5 for heating the crucible; an electrode device 10 which is accommodated in the crucible and has an anode 3 and a cathode 4; a power circuit 11 for electrolysis, for supplying a power source between the both electrodes of the electrode device; an electrode driving device for ascendably/descendably and rotatably driving a movable electrode of the electrode device; and a recovery device 21 for recovering electrolytic deposits deposited on a cathode side by the supply of the power source to the both electrodes. The recovery device is connected to a rotating mechanism 23 or a swinging mechanism, and the separation of a recovery metal 24 and the molten salt 2 is carried out by a force by rotation or swing of the rotating mechanism or the swinging mechanism.

Description

本発明は、使用済燃料の再処理を行なう乾式再処理技術に係り、特に、使用済燃料の中から有効成分を電解により電極に析出させて回収する溶融塩電解装置および溶融塩電解方法に関する。   The present invention relates to a dry reprocessing technique for reprocessing spent fuel, and more particularly to a molten salt electrolysis apparatus and a molten salt electrolysis method for collecting active components from spent fuel by electrolysis and collecting them on an electrode.

原子力発電所から発生する使用済燃料の溶融塩電解法を用いた再処理装置として、使用済燃料を陽極として電位をかけることにより、使用済燃料に含まれる核分裂生成物(FP)を除去し、燃料製造に必要な金属を陰極に析出させ、機械的手段を用いて掻き取り、それを回収容器にて収集し、以降の塩除去プロセスにて塩を取除き、金属燃料として成型・製造する技術が確立されている。   As a reprocessing device using the molten salt electrolysis method of spent fuel generated from nuclear power plants, the fission product (FP) contained in the spent fuel is removed by applying a potential using the spent fuel as an anode, Technology that deposits the metal required for fuel production on the cathode, scrapes it off using mechanical means, collects it in a recovery container, removes the salt in the subsequent salt removal process, and forms and manufactures it as metal fuel Is established.

図6は従来の使用済燃料を処理する溶融塩電解装置を模式的に示した縦断面図である。   FIG. 6 is a longitudinal sectional view schematically showing a conventional molten salt electrolysis apparatus for processing spent fuel.

図6において溶融塩電解装置1は、金属製のるつぼ14を有し、このるつぼ14内に溶融状態の塩2が収容され、溶融塩2中に陽極である陽極バスケット3と陰極である可動電極4が浸漬されている。溶融塩2は、例えば塩化ナトリウム、塩化カリウムのようなアルカリ金属の塩化物で形成される。るつぼ14の外周側には加熱ヒータ5が加熱手段として設けられている。加熱ヒータ5は、るつぼ14の外周側に保護容器を介して設けてもよい。加熱ヒータ5は、るつぼ14を例えば500℃〜700℃の高温に加熱するようになっている。   In FIG. 6, the molten salt electrolysis apparatus 1 has a crucible 14 made of metal, a molten salt 2 is accommodated in the crucible 14, and an anode basket 3 as an anode and a movable electrode as a cathode in the molten salt 2. 4 is immersed. The molten salt 2 is formed of an alkali metal chloride such as sodium chloride or potassium chloride. A heater 5 is provided on the outer peripheral side of the crucible 14 as a heating means. The heater 5 may be provided on the outer peripheral side of the crucible 14 via a protective container. The heater 5 heats the crucible 14 to a high temperature of, for example, 500 ° C to 700 ° C.

るつぼ14の頂部は、上蓋6で覆われ、るつぼ14内が閉塞されている。上蓋6には、筒状あるいはスリーブ状の断熱部材7を介して陽極バスケット3が設けられている。断熱部材7は筒状あるいは棒状をなし陽極バスケット3のサポートメンバとして機能する構成となっている。   The top of the crucible 14 is covered with the upper lid 6 and the inside of the crucible 14 is closed. The upper lid 6 is provided with an anode basket 3 via a cylindrical or sleeve-like heat insulating member 7. The heat insulating member 7 has a cylindrical shape or a bar shape and functions as a support member of the anode basket 3.

陽極バスケット3は金網やパンチングメタル等のメッシュ部材あるいは開口部材を円筒状、スリーブ状あるいはトーラス状のバスケット形状に組み立てたものであり、るつぼ14内の外周側に一方の電極を陽極として構成している。この陽極バスケット3の内側に逆截頭円錐形状の可動電極4が他方の電極(陰極)として設けられる。両電極3,4により電極装置10が構成される。   The anode basket 3 is formed by assembling a mesh member or an opening member such as a wire mesh or punching metal into a cylindrical, sleeve-like or torus-like basket shape. Yes. A movable electrode 4 having a reverse truncated cone shape is provided inside the anode basket 3 as the other electrode (cathode). The electrode device 10 is constituted by both the electrodes 3 and 4.

陽極バスケット3は、るつぼ14内の周方向に沿って設けられたトーラス状あるいは円環状、円筒状の固定電極であり、バスケット内部に被覆管付使用済切断燃料8が収納される。他方の電極4は、固定電極3の内側に同心円状に配置可能な可動電極を構成している。   The anode basket 3 is a torus-shaped, annular, or cylindrical fixed electrode provided along the circumferential direction in the crucible 14, and the spent cutting fuel 8 with a cladding tube is accommodated inside the basket. The other electrode 4 constitutes a movable electrode that can be arranged concentrically inside the fixed electrode 3.

両電極3,4には電解用電源11により電解用電源回路を介して電圧が印加され、一方の固定電極3は陽極として、他方の可動電極4は陰極として構成され、機能する。   A voltage is applied to both electrodes 3 and 4 via an electrolysis power supply circuit by an electrolysis power supply 11, and one fixed electrode 3 is configured as an anode and the other movable electrode 4 is configured as a cathode and functions.

さらに、るつぼ14内に設けられる陽極バスケット3の底部からサポート部材13が下方に延設され、このサポート部材13の先端に析出物の回収容器12が設けられている。サポート部材13はスリーブ状あるいは筒状メンバであっても、またロッド状メンバを複数本周方向に配設したものでもよい。サポート部材11には、析出物の掻き取り用カッタ9が取り付けられている。   Further, a support member 13 extends downward from the bottom of the anode basket 3 provided in the crucible 14, and a deposit collection container 12 is provided at the tip of the support member 13. The support member 13 may be a sleeve-shaped or cylindrical member, or may be a member in which a plurality of rod-shaped members are arranged in the circumferential direction. The support member 11 is provided with a cutter 9 for scraping off precipitates.

そして、両電極3,4にて電解を行い、陰極である可動電極4に金属を析出させ、掻き取り用カッタ9にて析出した金属を掻き取り、陰極下部に設置した回収容器12にて受取り、回収する。回収した金属が入った回収容器には昇降機構を有しており、電解完了後、溶融塩2から引き上げ、金属を回収する。電解により使用済燃料8の溶解を行い、金属U、Pu、マイナーアクチニド等を析出させ、析出した金属を回収する構成を有している。   Then, the electrodes 3 and 4 are electrolyzed, the metal is deposited on the movable electrode 4 serving as the cathode, the metal deposited on the scraping cutter 9 is scraped off, and is received by the collection container 12 installed under the cathode. ,to recover. The recovery container containing the recovered metal has an elevating mechanism, and after completion of electrolysis, the metal is recovered by pulling up from the molten salt 2. The spent fuel 8 is dissolved by electrolysis to deposit metals U, Pu, minor actinides and the like, and the deposited metals are collected.

特開2006−314958号公報JP 2006-314958 A

上述した使用済燃料を処理する溶融塩電解装置では、電解停止後に掻き取り、回収した金属が入った回収容器を溶融塩から引き上げる際に、回収容器に溶融塩が流入するため、回収する金属の他に金属に付着した不要な大量の塩も同時に回収することになる。このため、使用済み再処理工程における塩除去プロセスで、塩の蒸発除去に長時間の加熱が必要になると共に、処理単位に含まれる回収金属量が減ってしまい、処理時間、コスト、効率の面において課題が発生している。   In the molten salt electrolysis apparatus for processing the spent fuel described above, when the recovery container containing scraped metal that has been scraped and recovered is pulled from the molten salt, the molten salt flows into the recovery container. In addition, an unnecessary large amount of salt adhering to the metal is also recovered at the same time. For this reason, in the salt removal process in the used reprocessing step, heating for a long time is required for evaporating and removing the salt, and the amount of recovered metal contained in the processing unit is reduced, resulting in processing time, cost, and efficiency. There is a problem.

本発明は上述した課題を解決するためになされたものであり、後段の塩除去プロセスへの効率的な金属の供給が可能な機構を有した溶融塩電解装置および溶融塩電解方法を提供することを目的としている。   The present invention has been made to solve the above-described problems, and provides a molten salt electrolysis apparatus and a molten salt electrolysis method having a mechanism capable of efficiently supplying a metal to a subsequent salt removal process. It is an object.

本発明に係る溶融塩電解装置は、溶融塩を収納するるつぼと、このるつぼを加熱する加熱手段と、前記るつぼ内に収容され電解原料を収納し前記溶融塩が流通する陽極と前記溶融塩と接し電解析出物を析出させる陰極とを有する電極装置と、この電極装置の両電極間に電源を供給する電解用電源回路と、前記電極装置の可動電極を昇降可能かつ回転可能に駆動する電極駆動装置と、前記両電極に電源を供給することにより陰極側に析出する電解析出物を回収する回収装置とを有し、この回収装置は回転機構または振動機構に接続され、この回転機構または振動機構の回転または振動による力により回収金属と溶融塩の分離を行うことを特徴とする。   The molten salt electrolysis apparatus according to the present invention includes a crucible for storing molten salt, a heating means for heating the crucible, an anode stored in the crucible for storing an electrolytic raw material and flowing the molten salt, and the molten salt An electrode device having a cathode that contacts and deposits electrolytic deposits, an electrolysis power supply circuit that supplies power between both electrodes of the electrode device, and an electrode that drives the movable electrode of the electrode device to be movable up and down and rotatable A drive device and a recovery device for recovering electrolytic deposits deposited on the cathode side by supplying power to the electrodes, and the recovery device is connected to a rotation mechanism or a vibration mechanism. The recovered metal is separated from the molten salt by the force of rotation or vibration of the vibration mechanism.

また本発明に係る溶融塩電解方法は、溶融塩を収納するるつぼと、このるつぼを加熱する加熱手段と、前記るつぼ内に収容され電解原料を収納し前記溶融塩が流通する陽極と前記溶融塩と接し電解析出物を析出させる陰極とを有する電極装置と、この電極装置の両電極間に電源を供給する電解用電源回路と、前記電極装置の可動電極を昇降可能かつ回転可能に駆動する電極駆動装置と、前記両電極に電源を供給することにより陰極側に析出する電解析出物を回収する回収装置とを有する電解装置において、この回収装置はこの回収装置に接続された回転機構または振動機構の回転または振動による力により回収金属と溶融塩の分離を行うことを特徴とする。   Further, the molten salt electrolysis method according to the present invention includes a crucible for storing molten salt, a heating means for heating the crucible, an anode stored in the crucible for storing an electrolytic raw material and flowing the molten salt, and the molten salt An electrode device having a cathode in contact with the electrode for depositing electrolytic deposits, an electrolysis power supply circuit for supplying power between both electrodes of the electrode device, and a movable electrode of the electrode device being driven to be movable up and down and rotatable In an electrolysis apparatus having an electrode drive device and a recovery device that recovers electrolytic deposits deposited on the cathode side by supplying power to both electrodes, the recovery device is a rotating mechanism connected to the recovery device or The recovered metal is separated from the molten salt by the force of rotation or vibration of the vibration mechanism.

本発明の溶融塩電解装置および溶融塩電解方法によれば、使用済み再処理工程の電解によって回収金属が取り出された後段の塩除去プロセスにおいて、効率的に塩の除去が可能となると共に、処理単位の金属供給量の増加が可能となり、金属燃料製造の生産性を向上することができる。   According to the molten salt electrolysis apparatus and the molten salt electrolysis method of the present invention, in the subsequent salt removal process in which the recovered metal is taken out by electrolysis in the used reprocessing step, the salt can be efficiently removed and treated. The amount of metal supply per unit can be increased, and the productivity of metal fuel production can be improved.

本発明に係る溶融塩電解装置の第1の実施例を示す概略縦断面図。1 is a schematic longitudinal sectional view showing a first embodiment of a molten salt electrolysis apparatus according to the present invention. 本発明に係る溶融塩電解装置の第1の実施例の駆動状態を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the drive state of the 1st Example of the molten salt electrolysis apparatus which concerns on this invention. 本発明に係る溶融塩電解装置の第2の実施例を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the 2nd Example of the molten salt electrolysis apparatus which concerns on this invention. 本発明に係る溶融塩電解装置の第2の実施例の変形例を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the modification of the 2nd Example of the molten salt electrolysis apparatus which concerns on this invention. 本発明に係る溶融塩電解装置の第3の実施例を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the 3rd Example of the molten salt electrolysis apparatus which concerns on this invention. 溶融塩電解装置の従来例を示す概略縦断面図。The schematic longitudinal cross-sectional view which shows the prior art example of a molten salt electrolysis apparatus.

以下、本発明に係る溶融塩電解装置および溶融塩電解方法の実施の形態について、添付図面を参照して説明する。   Hereinafter, embodiments of a molten salt electrolysis apparatus and a molten salt electrolysis method according to the present invention will be described with reference to the accompanying drawings.

(第1の実施の形態)
図1および図2を参照して本発明の第1の実施の形態を説明する。なお、図1および図2において図6と同一部分には同一符号を付し、その部分の構成の説明は省略する。
(First embodiment)
A first embodiment of the present invention will be described with reference to FIGS. In FIG. 1 and FIG. 2, the same parts as those in FIG.

図1は、本発明の第1の実施の形態における溶融塩電解装置の構成を示しており、図2は図1示した溶融塩電解装置の駆動状態を示している。   FIG. 1 shows the configuration of the molten salt electrolysis apparatus according to the first embodiment of the present invention, and FIG. 2 shows the driving state of the molten salt electrolysis apparatus shown in FIG.

本発明の第1の実施の形態における溶融塩電解装置20は、加熱ヒータ5により室温から700℃程度まで加熱が可能なるつぼ14を有し、このるつぼ14内に溶融状態の塩2が収納され、溶融塩2中に昇降可能な陽極3と陰極4が浸漬されている。   The molten salt electrolysis apparatus 20 in the first embodiment of the present invention has a crucible 14 that can be heated from room temperature to about 700 ° C. by the heater 5, and the molten salt 2 is accommodated in the crucible 14. The anode 3 and the cathode 4 that can be moved up and down are immersed in the molten salt 2.

この溶融塩2は例えば塩化ナトリウム、塩化カルシウム、塩化リチウム、塩化カリウムのようなアルカリ金属の塩化物もしくはこれらの混合塩で形成されている。陽極3はメッシュ部材等のバスケット形状であり、バスケット内部に使用済燃料8が収納されている。溶融塩2に浸漬した金属の回収容器21は、電極3,4とは独立に支持部材22によって支持されており、かつ、高速回転することが可能なように回転駆動用モータ23に接続されている。   The molten salt 2 is formed of an alkali metal chloride such as sodium chloride, calcium chloride, lithium chloride or potassium chloride, or a mixed salt thereof. The anode 3 has a basket shape such as a mesh member, and spent fuel 8 is accommodated inside the basket. The metal recovery container 21 immersed in the molten salt 2 is supported by a support member 22 independently of the electrodes 3 and 4 and connected to a rotation drive motor 23 so as to be able to rotate at high speed. Yes.

このように構成された本発明の第1の実施の形態において、回収容器21が支持部材22を介して回転駆動用モータ23に接続されているため、電解処理の停止後に図2に示すように回収容器21を溶融塩2中から引き上げ、回収容器21を図中矢印A方向に高速回転させることにより、図6に示す掻き取り用カッタによって可動電極4の周囲に付着され掻き取られ回収容器21内に収容された回収金属24に付着した塩の大部分を、遠心力によって回収容器21内からるつぼ14に排出させて取除くことができる。   In the first embodiment of the present invention configured as described above, the collection container 21 is connected to the rotation drive motor 23 via the support member 22, so that the electrolytic treatment is stopped as shown in FIG. By pulling up the recovery container 21 from the molten salt 2 and rotating the recovery container 21 at a high speed in the direction of arrow A in the figure, the recovery container 21 is attached to the periphery of the movable electrode 4 by the scraping cutter shown in FIG. Most of the salt adhering to the recovered metal 24 accommodated in the container can be removed by being discharged from the recovery container 21 to the crucible 14 by centrifugal force.

よって、使用済み再処理工程の電解によって回収金属が取り出された後段の塩除去プロセスにおいて、効率的に塩の除去が可能になると共に、処理単位の金属供給量の増加が可能となり、金属燃料製造の生産性を向上させることができる。   Therefore, in the subsequent salt removal process in which the recovered metal is removed by electrolysis in the used reprocessing step, it is possible to efficiently remove the salt and increase the amount of metal supplied to the processing unit, thereby producing metal fuel. Productivity can be improved.

また、回収金属と付着した塩との分離方法として、回収容器21に回転機構23を設けたものではなく、例えば、回収容器21に小刻みに昇降動作(振動)可能なシリンダの支持棒(図示せず)を設け、回収容器21の底部及び側面を微細なメッシュ部材もしくはパンチングメタル等とし、回収容器21が小刻みに昇降(振動)動作することにより、回収金属に付着した塩を大部分分離する構成としても良い。   In addition, as a method for separating the recovered metal and the attached salt, the recovery container 21 is not provided with the rotation mechanism 23. The bottom and side surfaces of the recovery container 21 are made of fine mesh members or punching metal, etc., and the recovery container 21 moves up and down (vibrates) in small increments to largely separate the salt adhering to the recovery metal. It is also good.

(第2の実施の形態)
図3および図4を参照して本発明の第2の実施の形態を説明する。なお、図3および図4において図1と同一部分には同一符号を付し、その部分の構成の説明は省略する。
(Second Embodiment)
A second embodiment of the present invention will be described with reference to FIGS. 3 and 4, the same parts as those in FIG. 1 are denoted by the same reference numerals, and description of the structure of those parts is omitted.

第1の実施の形態では、回収金属24とそれに付着した塩2の分離を行うため、回収容器21に回転機構23もしくは昇降機構を設けることにより分離を行うが、第2の実施の形態としては回収金属24と塩2との分離方法として、回収容器21を加熱することにより、回収金属24とそれに付着した塩2の分離を行う方法とし、その構成を図3および図4に示す。   In the first embodiment, in order to separate the recovered metal 24 and the salt 2 adhering thereto, separation is performed by providing the recovery container 21 with a rotation mechanism 23 or an elevating mechanism. However, as the second embodiment, As a method for separating the recovered metal 24 and the salt 2, a method for separating the recovered metal 24 and the salt 2 attached thereto by heating the recovery container 21 is shown in FIGS. 3 and 4.

図3の溶融塩電解装置30は、電解停止後の陽極3、陰極4の引き抜き時にるつぼ14の頂部に保温材18を装着し、この保温材18を貫通して設けられた吊り部材17に吊設された回収容器用ヒータ19を回収容器21の開口部に装着する構成である。この回収容器用ヒータ19により、回収容器21を塩2のみが蒸発する温度800℃〜1000℃程度に昇温させ、回収容器用ヒータ19に形成された放出孔16から放出させることにより塩2を気化させ回収容器21内から取除くことが可能である。 The molten salt electrolysis apparatus 30 in FIG. 3 has a heat insulating material 18 attached to the top of the crucible 14 when the anode 3 and the cathode 4 after the electrolysis is stopped, and is suspended by a suspension member 17 provided through the heat insulating material 18. The provided collection container heater 19 is attached to the opening of the collection container 21. The recovery container heater 19 raises the temperature of the recovery container 21 to about 800 ° C. to 1000 ° C. at which only the salt 2 evaporates, and releases the salt 2 from the discharge hole 16 formed in the recovery container heater 19. It can be vaporized and removed from the collection container 21.

また、上述の回収容器21の加熱方法として、回収容器用ヒータ19ではなく、例えば図4に第2の実施の形態の変形例として示すようにマイクロ波印加装置31を設け、回収容器21に導波管32からコネクタ33を介してマイクロ波Bを印加させることにより溶融塩2を加熱し蒸発させ、放出孔16から放出させることにより回収金属24とそれに付着した大量の塩2を分離することができる溶融塩電解装置30でも可能である。   In addition, as a heating method of the recovery container 21 described above, instead of the recovery container heater 19, for example, a microwave application device 31 is provided as shown in FIG. 4 as a modification of the second embodiment to guide the recovery container 21. By applying microwave B from the wave tube 32 through the connector 33, the molten salt 2 is heated and evaporated, and discharged from the discharge hole 16, thereby separating the recovered metal 24 and a large amount of the salt 2 attached thereto. A possible molten salt electrolysis apparatus 30 is also possible.

よって、使用済み再処理工程の電解によって回収金属が取り出された後段の塩除去プロセスにおいて、効率的に塩の除去が可能になると共に、処理単位の金属供給量の増加が可能となり、金属燃料製造の生産性を向上させることができる。さらには駆動部分を少なくすることによって故障の確率の低い信頼性の高い溶融塩電解装置とすることができる。   Therefore, in the subsequent salt removal process in which the recovered metal is removed by electrolysis in the used reprocessing step, it is possible to efficiently remove the salt and increase the amount of metal supplied to the processing unit, thereby producing metal fuel. Productivity can be improved. Furthermore, by reducing the number of drive parts, a highly reliable molten salt electrolyzer with a low probability of failure can be obtained.

(第3の実施の形態)
図5を参照して本発明の第3の実施の形態を説明する。なお、図5において図1と同一部分には同一符号を付し、その部分の構成の説明は省略する。
(Third embodiment)
A third embodiment of the present invention will be described with reference to FIG. In FIG. 5, the same parts as those in FIG. 1 are denoted by the same reference numerals, and description of the structure of those parts is omitted.

図5の溶融塩電解装置40は、第1の実施の形態に示した陽極バスケット3の支持棒41が中空構造となっており、この中空の支持棒41に配設されたバルブ42を開けることにより、溶融塩電解装置40の本体上部に設置された使用済燃料貯槽43から使用済燃料8を供給することができる。 In the molten salt electrolyzer 40 of FIG. 5, the support bar 41 of the anode basket 3 shown in the first embodiment has a hollow structure, and the valve 42 disposed on the hollow support bar 41 is opened. Thus, the spent fuel 8 can be supplied from the spent fuel storage tank 43 installed in the upper part of the main body of the molten salt electrolyzer 40.

このように構成された溶融塩電解装置40において、電解を行い、初期に陽極バスケット3に入れた使用済燃料8が陰極4に析出し、電解が進むにつれて陽極バスケット3内の使用済燃料8が減少していき、電解速度が低下した場合、陽極バスケット3上部のバルブ42を開動作させ、未処理の使用済燃料8を供給することができる。   In the molten salt electrolyzer 40 configured as described above, electrolysis is performed, and the spent fuel 8 initially placed in the anode basket 3 is deposited on the cathode 4, and as the electrolysis proceeds, the spent fuel 8 in the anode basket 3 is When the rate of electrolysis decreases, the valve 42 above the anode basket 3 is opened, and the unprocessed spent fuel 8 can be supplied.

このことにより、電解速度をほぼ一定にして、使用済燃料を電解処理させることができる。よって、電解効率及び生産性を向上させることができる。   As a result, the spent fuel can be electrolyzed with the electrolysis rate kept substantially constant. Therefore, electrolytic efficiency and productivity can be improved.

なお、溶融塩電解法を用いた使用済燃料の再処理プロセスにおいて、軽水炉等から発生する使用済燃料は酸化物の形態であるため、一般的には、上述の金属精製プロセスの前段に酸化物を金属に還元する電解還元プロセスがある。本実施の形態で示した使用済燃料供給機構は、金属精製プロセスに限らず、電解還元プロセスで使用する装置にも同様に設置し、生産性の向上となる効果を発揮することが可能である。   Note that, in the spent fuel reprocessing process using the molten salt electrolysis method, spent fuel generated from a light water reactor or the like is in the form of an oxide. There is an electrolytic reduction process that reduces the metal to metal. The spent fuel supply mechanism shown in the present embodiment is not limited to the metal refining process, and can be similarly installed in an apparatus used in the electrolytic reduction process, and can exhibit the effect of improving productivity. .

1,20,30,40…溶融塩電解装置、2…溶融塩、3…陽極バスケット(陽極)、4…可動電極(陰極)、5…加熱ヒータ(加熱手段)、6…上蓋、7…断熱部材、8…被覆管付使用済切断燃料(使用済燃料)、9…掻き取り用カッタ、10…電極装置、11…電解用電源、12,21…回収容器、13…サポート部材、14…るつぼ、16…放出孔、17…吊り部材、18…保温材、19…回収容器用ヒータ、22…支持部材、23…回転駆動用モータ(回転機構)、24…回収金属、31…マイクロ波印加装置、32…導波管、33…コネクタ、41…支持棒、42…バルブ、43…使用済燃料貯槽。 DESCRIPTION OF SYMBOLS 1,20,30,40 ... Molten salt electrolysis apparatus, 2 ... Molten salt, 3 ... Anode basket (anode), 4 ... Movable electrode (cathode), 5 ... Heating heater (heating means), 6 ... Top cover, 7 ... Thermal insulation 8: Used cutting fuel with a cladding tube (spent fuel), 9: Cutter for scraping, 10 ... Electrode device, 11 ... Power supply for electrolysis, 12, 21 ... Recovery container, 13 ... Support member, 14 ... Crucible , 16 ... discharge hole, 17 ... suspension member, 18 ... heat insulating material, 19 ... heater for recovery container, 22 ... support member, 23 ... motor for rotation drive (rotation mechanism), 24 ... recovery metal, 31 ... microwave application device 32 ... Waveguide, 33 ... Connector, 41 ... Support rod, 42 ... Valve, 43 ... Spent fuel storage tank.

Claims (7)

溶融塩を収納するるつぼと、
このるつぼを加熱する加熱手段と、
前記るつぼ内に収容され、電解原料を収納し前記溶融塩が流通する陽極と、前記溶融塩と接し電解析出物を析出させる陰極と、を有する電極装置と、
この電極装置の両電極間に電源を供給する電解用電源回路と、
前記電極装置の可動電極を昇降可能かつ回転可能に駆動する電極駆動装置と、
前記両電極に電源を供給することにより陰極側に析出する電解析出物を回収する回収装置とを有し、
この回収装置は回転機構または振動機構に接続され、この回転機構または振動機構の回転または振動による力により回収金属と溶融塩の分離を行うことを特徴とする溶融塩電解装置。
A crucible for storing molten salt;
Heating means for heating the crucible;
An electrode device housed in the crucible, containing an electrolytic raw material and through which the molten salt flows, and a cathode in contact with the molten salt to deposit electrolytic deposits;
An electrolysis power supply circuit for supplying power between both electrodes of the electrode device;
An electrode driving device for driving the movable electrode of the electrode device to be movable up and down and rotatable;
A recovery device for recovering electrolytic deposits deposited on the cathode side by supplying power to both electrodes;
The recovery apparatus is connected to a rotation mechanism or a vibration mechanism, and the recovered metal and the molten salt are separated by a force generated by the rotation or vibration of the rotation mechanism or the vibration mechanism.
前記回収容器の底部及び側面を網部材もしくはパンチングメタルで形成したことを特徴とする請求項1記載の溶融塩電解装置。   2. The molten salt electrolysis apparatus according to claim 1, wherein the bottom and side surfaces of the recovery container are formed of a net member or punching metal. 前記回転機構に代えて、前記回収容器を引き上げた際に前記加熱手段とは別に上部から回収容器を覆うことができるヒータを有し、このヒータはるつぼ内で前記回収容器を塩 のみが蒸発される温度まで昇温させ、気化した塩が回収容器の開口部を通り回収容器外へ排気されることを特徴とする請求項1記載の溶融塩電解装置。   In place of the rotating mechanism, when the collection container is pulled up, it has a heater that can cover the collection container from the top separately from the heating means, and this heater evaporates only the salt in the collection container in the crucible. The molten salt electrolysis apparatus according to claim 1, wherein the evaporated salt is exhausted out of the recovery container through the opening of the recovery container. 前記回転機構に代えて、前記回収容器を引き上げた際に前記加熱手段とは別に上部から回収容器を覆うことができるマイクロ波加熱装置を有し、このマイクロ波加熱装置はる つぼ内で前記回収容器を塩のみが蒸発される温度まで昇温させ、気化した塩が回収容器の開口部を通り回収容器外へ排気されることを特徴とする請求項1記載の溶融塩電解装
置。
In place of the rotating mechanism, when the collection container is pulled up, it has a microwave heating device that can cover the collection container from the top separately from the heating means, and the microwave heating apparatus is used in the crucible to collect the collection container. 2. The molten salt electrolysis device according to claim 1, wherein the temperature of the container is raised to a temperature at which only the salt is evaporated, and the vaporized salt is exhausted out of the recovery container through the opening of the recovery container.
前記陽極は電解原料を収納する貯槽からこの電解原料が供給されることを特徴とする請求項1から3のいずれか1項記載の溶融塩電解装置。   4. The molten salt electrolysis apparatus according to claim 1, wherein the anode is supplied with an electrolytic raw material from a storage tank that stores the electrolytic raw material. 5. 溶融塩を収納するるつぼと、
このるつぼを加熱する加熱手段と、
前記るつぼ内に収容され、電解原料を収納し前記溶融塩が流通する陽極と、前記溶融塩と接し電解析出物を析出させる陰極、とを有する電極装置と、
この電極装置の両電極間に電源を供給する電解用電源回路と、
前記電極装置の可動電極を昇降可能かつ回転可能に駆動する電極駆動装置と、
前記両電極に電源を供給することにより陰極側に析出する電解析出物を回収する回収装置とを有する電解装置において、
この回収装置はこの回収装置に接続された回転機構または振動機構の回転または振動による力により回収金属と溶融塩の分離を行うことを特徴とする溶融塩電解方法。
A crucible for storing molten salt;
Heating means for heating the crucible;
An electrode device housed in the crucible, containing an electrolytic raw material and through which the molten salt flows, and a cathode in contact with the molten salt to deposit electrolytic deposits;
An electrolysis power supply circuit for supplying power between both electrodes of the electrode device;
An electrode driving device for driving the movable electrode of the electrode device to be movable up and down and rotatable;
In an electrolytic device having a recovery device for recovering electrolytic deposits deposited on the cathode side by supplying power to both electrodes,
This recovery apparatus is a molten salt electrolysis method characterized in that the recovered metal and the molten salt are separated by a force generated by rotation or vibration of a rotation mechanism or a vibration mechanism connected to the recovery apparatus.
溶融塩を収納するるつぼと、
このるつぼを加熱する加熱手段と、
前記るつぼ内に収容され、電解原料を収納し前記溶融塩が流通する陽極と、前記溶融塩と接し電解析出物を析出させる陰極と、を有する電極装置と、
この電極装置の両電極間に電源を供給する電解用電源回路と、
前記電極装置の可動電極を昇降可能かつ回転可能に駆動する電極駆動装置と、
前記両電極に電源を供給することにより陰極側に析出する電解析出物を回収する回収装置とを有する電解装置において、
この回収装置はこの回収装置の上部を覆う加熱装置によって前記溶融塩を蒸発させて回収金属と溶融塩の分離を行うことを特徴とする溶融塩電解方法。
A crucible for storing molten salt;
Heating means for heating the crucible;
An electrode device housed in the crucible, containing an electrolytic raw material and through which the molten salt flows, and a cathode in contact with the molten salt to deposit electrolytic deposits;
An electrolysis power supply circuit for supplying power between both electrodes of the electrode device;
An electrode driving device for driving the movable electrode of the electrode device to be movable up and down and rotatable;
In an electrolytic device having a recovery device for recovering electrolytic deposits deposited on the cathode side by supplying power to both electrodes,
The recovery apparatus electrolyzes the molten salt by evaporating the molten salt by a heating device that covers an upper portion of the recovery apparatus to separate the recovered metal and the molten salt.
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