JPH10293193A - Molten salt electrolysis device - Google Patents
Molten salt electrolysis deviceInfo
- Publication number
- JPH10293193A JPH10293193A JP10172297A JP10172297A JPH10293193A JP H10293193 A JPH10293193 A JP H10293193A JP 10172297 A JP10172297 A JP 10172297A JP 10172297 A JP10172297 A JP 10172297A JP H10293193 A JPH10293193 A JP H10293193A
- Authority
- JP
- Japan
- Prior art keywords
- liquid metal
- molten salt
- cathode
- container
- uranium
- 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.)
- Granted
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Electrolytic Production Of Metals (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、ウランを含む使用
済核燃料を再処理・回収するための溶融塩電解装置に関
するものである。TECHNICAL FIELD The present invention relates to a molten salt electrolysis apparatus for reprocessing and recovering spent nuclear fuel containing uranium.
【０００２】[0002]
【従来の技術】従来、使用済核燃料の乾式再処理装置で
ある溶融塩電解装置では使用済核燃料をバスケットに入
れて電解槽の下部に貯留された液体Ｃｄの中に投入する
か、又は図４に示すように使用済核燃料２をバスケット
３に入れて電解槽１の溶融塩６の中で保持し、液体Ｃｄ
又はバスケットを陽極としている。一方、溶融塩６中に
は固体陰極４及び容器８に貯留された液体Ｃｄ陰極７が
保持される。このような装置で溶融塩電解を行うと、先
ず溶融塩６に溶解しているウランイオンが矢印Ａで示す
ように、固体陰極４にデンドライド状の金属ウラン５と
なって分離回収される。次いで、溶融塩６中に残存され
るウランや濃縮されたプルトニウム、超ウラン元素（Ａ
ｍ，Ｃｍ等）が矢印Ｂで示すように、液体Ｃｄ陰極７中
に電解還元され回収される。このような水を用いない乾
式法により使用済核燃料を再処理することにより、再処
理プロセスが簡素化され、水を用いた湿式法により再処
理する場合に比較して再処理費用を低減できることが期
待されている。2. Description of the Related Art Conventionally, in a molten salt electrolysis apparatus which is a dry reprocessing apparatus for spent nuclear fuel, spent nuclear fuel is put into a basket and poured into a liquid Cd stored in a lower portion of an electrolytic cell, or FIG. The spent nuclear fuel 2 is put in the basket 3 and held in the molten salt 6 of the electrolytic cell 1 as shown in FIG.
Alternatively, the basket is used as the anode. On the other hand, the solid cathode 4 and the liquid Cd cathode 7 stored in the container 8 are held in the molten salt 6. When the molten salt electrolysis is performed by such an apparatus, first, uranium ions dissolved in the molten salt 6 are separated and recovered as dendritic metal uranium 5 on the solid cathode 4 as shown by an arrow A. Next, the uranium remaining in the molten salt 6, the concentrated plutonium, and the transuranium element (A
m, Cm, etc.) are electrolytically reduced and collected in the liquid Cd cathode 7 as shown by the arrow B. By reprocessing spent nuclear fuel by such a dry method without water, the reprocessing process can be simplified, and the cost of reprocessing can be reduced compared to the case of reprocessing by a wet method using water. Expected.
【０００３】[0003]
【発明が解決しようとする課題】しかし、上述した乾式
再処理では固体陰極４にデンドライド状のウラン５を容
易に析出させ回収することができる一方、液体Ｃｄ陰極
７ではウランを電解還元する際にウランが液体Ｃｄ陰極
７の表面に結晶として成長し、その成長した結晶に電流
が集中してデンドライド状のウランのみが異常に成長
し、溶融塩６中に濃縮されたプルトニウムはその析出が
阻害され、正常な電解を行うことができなかった。However, in the dry reprocessing described above, dendritic uranium 5 can be easily precipitated and recovered on the solid cathode 4, while the liquid Cd cathode 7 is not suitable for electrolytic reduction of uranium. Uranium grows as a crystal on the surface of the liquid Cd cathode 7, current concentrates on the grown crystal, and only dendritic uranium grows abnormally, and the precipitation of plutonium concentrated in the molten salt 6 is inhibited. , Normal electrolysis could not be performed.
【０００４】この点を解消するために液体Ｃｄ陰極７に
容器８の上部から撹拌インペラ（図示せず）を浸漬し、
液体Ｃｄ陰極７をこのインペラで撹拌し、液体Ｃｄを回
転させながら液体Ｃｄ陰極７の上面に還元析出した核燃
料物質を機械的に液体Ｃｄ陰極７の内部に混合分散させ
ることが試みられている。しかし、単に、陰極７の液体
Ｃｄを回転させるだけでは結晶として成長したウランが
液体Ｃｄ陰極７とともに回転するだけで液体Ｃｄ陰極７
の内部に混合分散されない不具合がある。この場合、陰
極電流密度を低下させることやインペラの回転数を増大
させることが考えられるが、陰極電流密度を低下させる
と処理能力の低下を招き、インペラの回転数を増大させ
ると、その遠心力により容器８の内壁面に密度の高いウ
ランデンドライド粒子が濃縮され、これが内壁面上部ま
で付着することとなり、電解を長時間行うときには液体
Ｃｄ陰極７の上面にウランデンドライドが成長する恐れ
もある。In order to solve this problem, a stirring impeller (not shown) is immersed in the liquid Cd cathode 7 from the upper part of the container 8.
Attempts have been made to stir the liquid Cd cathode 7 with this impeller and mechanically mix and disperse the nuclear fuel material reduced and deposited on the upper surface of the liquid Cd cathode 7 inside the liquid Cd cathode 7 while rotating the liquid Cd. However, simply rotating the liquid Cd of the cathode 7 causes the uranium grown as a crystal to rotate together with the liquid Cd cathode 7, and the liquid Cd cathode 7
There is a problem that it is not mixed and dispersed inside. In this case, it is conceivable to reduce the cathode current density or increase the rotation speed of the impeller.However, if the cathode current density is reduced, the processing capacity is reduced, and if the rotation speed of the impeller is increased, the centrifugal force is increased. As a result, high-density uranium dendride particles are concentrated on the inner wall surface of the container 8 and adhere to the upper part of the inner wall surface. When electrolysis is performed for a long time, uranium dendride may grow on the upper surface of the liquid Cd cathode 7. .
【０００５】本発明の目的は、ウランが液体金属陰極表
面に成長することを防止して、電解還元によるウラン、
プルトニウム及び超ウラン元素の回収を安定に行う溶融
塩電解装置を提供することにある。本発明の別の目的
は、液体金属陰極上面に還元析出した物質を容器下部に
有効に沈降させる溶融塩電解装置を提供することにあ
る。An object of the present invention is to prevent uranium from growing on the surface of a liquid metal cathode, and to reduce uranium by electrolytic reduction.
An object of the present invention is to provide a molten salt electrolysis apparatus that stably recovers plutonium and transuranium elements. Another object of the present invention is to provide a molten salt electrolysis apparatus for effectively causing a substance reduced and deposited on the upper surface of a liquid metal cathode to settle in a lower portion of a container.
【０００６】[0006]
【課題を解決するための手段】請求項１に係る発明は、
図１に示すように、電解槽１１の内部に、使用済核燃料
に導通する陽極１２と、使用済核燃料中の少なくともウ
ランを溶解可能な溶融塩１３と、溶融塩中に配置された
容器１４に貯留された液体金属からなる陰極１６とを備
え、溶融塩電解により溶融塩１３中に溶解したウランを
液体金属１６中に析出させるように構成された溶融塩電
解装置の改良である。その特徴ある構成は、容器１４に
貯留された液体金属１６に浸漬するように上部より鉛直
下方に延びて設けられた回転軸１７と、回転軸１７の下
部に取付けられた液体金属撹拌用のインペラ１８と、イ
ンペラ１８を包囲するように容器１４内部に設けられた
筒体１９とを備えたところにある。回転軸１７の回転に
よりインペラ１８は液体金属１６を筒体１９の下部から
吸上げて筒体１９の上部から流出させる循環流を形成す
るため、筒体１９の外側で下方に向う液体金属１６の流
れが発生し、液体金属陰極の上面に析出したウラン等の
金属は液体金属１６の流れに従って液体金属１６中に沈
降する。The invention according to claim 1 is
As shown in FIG. 1, inside an electrolytic cell 11, an anode 12 that communicates with spent nuclear fuel, a molten salt 13 that can dissolve at least uranium in spent nuclear fuel, and a container 14 that is disposed in the molten salt are provided. The present invention is an improvement of a molten salt electrolysis apparatus including a cathode 16 made of stored liquid metal and configured to precipitate uranium dissolved in the molten salt 13 in the liquid metal 16 by molten salt electrolysis. Its characteristic configuration is that a rotating shaft 17 is provided extending vertically downward from the upper portion so as to be immersed in the liquid metal 16 stored in the container 14, and a liquid metal stirring impeller attached to the lower portion of the rotating shaft 17. 18 and a cylindrical body 19 provided inside the container 14 so as to surround the impeller 18. Due to the rotation of the rotation shaft 17, the impeller 18 forms a circulating flow in which the liquid metal 16 is sucked up from the lower part of the cylindrical body 19 and flows out from the upper part of the cylindrical body 19, so that the liquid metal 16 flowing downwardly outside the cylindrical body 19 A flow occurs, and the metal such as uranium deposited on the upper surface of the liquid metal cathode sediments in the liquid metal 16 according to the flow of the liquid metal 16.
【０００７】請求項２に係る発明は、請求項１に係る発
明であって、筒体１９が容器内部で上下動可能に構成さ
れた電解還元装置である。請求項３に係る発明は、請求
項１に係る発明であって、筒体１９と回転軸１７とが容
器１４内部で上下方向に連動可能に構成された電解還元
装置である。筒体１９を容器内部で上下動可能に構成
し、図３に示すように、筒体１９の上部を液体金属表面
から上方に突出させれば、陰極１６である液体金属の上
面、即ち電流の集中する部分を制御することができ、回
転軸１７を容器１４内部で上下方向に筒体１９と連動さ
せることにより、筒体１９を上下動させた場合であって
も液体金属１６を筒体１９の下部から有効に吸上げる。A second aspect of the present invention is the electrolytic reduction apparatus according to the first aspect, wherein the cylindrical body 19 is configured to be vertically movable inside the container. The invention according to claim 3 is the invention according to claim 1, which is an electrolytic reduction device in which the cylindrical body 19 and the rotating shaft 17 are configured to be vertically interlockable inside the container 14. The cylindrical body 19 is configured to be able to move up and down inside the container, and as shown in FIG. The concentrated portion can be controlled, and by rotating the rotating shaft 17 vertically with the cylinder 19 inside the container 14, the liquid metal 16 can be moved even when the cylinder 19 is moved up and down. Effectively sucks from the bottom.
【０００８】[0008]
【発明の実施の形態】次に本発明の実施の形態を図面に
基づいて説明する。図１に示すように、本発明の溶融塩
電解装置１０は電解槽１１の内部に使用済核燃料に導通
する陽極１２と、使用済核燃料中の少なくともウランを
溶解可能な溶融塩１３と、この溶融塩１３中に配置され
た容器１４に貯留された液体金属からなる陰極１６とを
備える。この装置の電解槽１１は蓋１１ａを有する鋼鉄
製の槽であって、槽底部には溶融されたカドミウムが貯
留され、この溶融カドミウムには上方から棒状の黒鉛製
の電極１２ａが絶縁被覆された状態で挿入され、この電
極１２ａを介して溶融カドミウムが陽極１２を構成する
ようになっている。電解槽１１の蓋１１ａには電解槽１
１に貯留された陽極１２を撹拌するための陽極用インペ
ラ１２ｂが回転可能に設けられ、このインペラ１２ｂを
回転させることにより陽極１２である溶融カドミウムを
撹拌できるようになっている。Embodiments of the present invention will now be described with reference to the drawings. As shown in FIG. 1, a molten salt electrolysis apparatus 10 of the present invention includes an anode 12 that communicates with spent nuclear fuel in an electrolytic cell 11, a molten salt 13 that can dissolve at least uranium in spent nuclear fuel, A cathode 16 made of a liquid metal stored in a container 14 disposed in the salt 13. The electrolytic cell 11 of this apparatus is a steel tank having a lid 11a, in which molten cadmium is stored at the bottom of the cell, and the molten cadmium is covered with a rod-shaped graphite electrode 12a from above. In this state, the molten cadmium forms the anode 12 via the electrode 12a. The lid 11a of the electrolytic cell 11 has an electrolytic cell 1
An anode impeller 12b for stirring the anode 12 stored in 1 is rotatably provided. By rotating the impeller 12b, molten cadmium as the anode 12 can be stirred.
【０００９】この陽極１２である溶融カドミウムの上部
にはウランを溶解可能な溶融塩１３が貯留される。液体
金属からなる陰極１６を貯留する容器１４は電解槽１１
の蓋１１ａに複数の支軸１４ａ，１４ａを介して溶融塩
１３の中に垂設される。容器１４は有底円筒状の黒鉛製
の容器であり、溶融カドミウムを貯留する。この容器１
４には上方から棒状の金属製の電極１６ａが絶縁被覆さ
れた状態で挿入され、この電極１６ａを介して容器１４
に貯留された溶融カドミウムが陰極１６を構成するよう
になっている。なお図示しないが、電解槽１１の外側に
は槽内を所定の温度に加熱維持するための加熱コイルが
設けられる。A molten salt 13 capable of dissolving uranium is stored above the molten cadmium serving as the anode 12. The container 14 for storing the cathode 16 made of liquid metal is the electrolytic cell 11.
Is suspended in the molten salt 13 via a plurality of support shafts 14a, 14a. The container 14 is a bottomed cylindrical container made of graphite, and stores molten cadmium. This container 1
A rod-shaped metal electrode 16a is inserted into the container 4 from above in a state where the electrode 16a is insulated and covered.
The molten cadmium stored in the cathode constitutes the cathode 16. Although not shown, a heating coil for heating and maintaining the inside of the tank at a predetermined temperature is provided outside the electrolytic tank 11.
【００１０】容器１４上方の電解槽１１の蓋１１ａには
容器１４に貯留された液体金属１６に浸漬するように上
部より回転軸１７が鉛直下方に延びて回転可能にかつ上
下動可能に設けられ、この回転軸１７の下部には液体金
属撹拌用のインペラ１８が取付けられる。また、蓋１１
ａには筒体１９が複数の支持棒１９ａ，１９ａを介して
容器１４内部でインペラ１８を包囲するように上下動可
能に設けられる。本実施の形態におけるインペラ１８は
モリブデンからなり、筒体１９はイットリア（Ｙ2Ｏ3）
の成型体又は窒化ホウ素（ＢＮ）の切削加工体である。
インペラ１８は所定の傾斜角度を有する羽根を複数枚設
けることにより構成される。このインペラ１８は回転軸
１７の回転により筒体１９の内部で回転し、図の実線矢
印で示すように、陰極１６である液体金属を筒体１９の
下部から吸上げて筒体１９の上部から流出するように構
成される。On the lid 11a of the electrolytic cell 11 above the container 14, a rotary shaft 17 extends vertically downward from the upper part so as to be immersed in the liquid metal 16 stored in the container 14 so as to be rotatable and vertically movable. An impeller 18 for stirring the liquid metal is mounted below the rotating shaft 17. Also, the lid 11
In a, a cylindrical body 19 is provided movably up and down so as to surround the impeller 18 inside the container 14 via a plurality of support rods 19a, 19a. In this embodiment, the impeller 18 is made of molybdenum, and the cylinder 19 is made of yttria (Y 2 O 3 ).
Or a boron nitride (BN) cut body.
The impeller 18 is configured by providing a plurality of blades having a predetermined inclination angle. The impeller 18 rotates inside the cylindrical body 19 by the rotation of the rotating shaft 17, and sucks the liquid metal as the cathode 16 from the lower part of the cylindrical body 19 and raises the liquid metal as the cathode 16 from the upper part of the cylindrical body 19 as shown by the solid arrow in the figure. Configured to spill.
【００１１】このような装置１０では図示しない加熱コ
イルに通電して電解槽１１を加熱し、槽内部の物質を溶
融した状態にした後、電解槽１１下部のＣｄ陽極１２中
に使用済の金属燃料を投入し、陰極１６及び陽極１２に
通電して溶融塩電解を実施すると、溶融塩１３中に溶解
したウラン、プルトニウム及び超ウラン元素（Ａｍ，Ｃ
ｍ等）の各陽イオンが図の破線矢印で示すように容器１
４内の液体Ｃｄ陰極１６に引寄せられ、これらの金属が
容器１４内の液体Ｃｄ陰極１６中に電解還元され回収さ
れる。In such an apparatus 10, a heating coil (not shown) is energized to heat the electrolytic cell 11 to melt the substance in the cell, and the used metal is placed in the Cd anode 12 below the electrolytic cell 11. When the fuel is supplied, and the cathode 16 and the anode 12 are energized to perform molten salt electrolysis, uranium, plutonium and transuranium elements (Am, C
m etc.) as shown by the dashed arrows in the figure.
The metal is attracted to the liquid Cd cathode 16 in 4, and these metals are electrolytically reduced and recovered in the liquid Cd cathode 16 in the container 14.
【００１２】溶融塩１３中に溶解したウラン、プルトニ
ウム等は、初めは液体Ｃｄ陰極１６の表面で還元析出す
る。ここで、図２に示すように、回転軸１７を回転させ
ることによりインペラ１８が筒体１９の内部で回転し、
陰極１６である液体金属が図の実線矢印で示すように、
筒体１９の下部から吸上げられて筒体１９の上部から流
出した後、筒体１９の外側で下方に向う流れを発生させ
る。この液体金属１６の流れは液体Ｃｄ陰極１６上面に
還元析出したウラン、プルトニウム等の金属を容器１４
下部に沈降させ、ウランが液体Ｃｄ陰極１６表面で結晶
成長することを防止する。Uranium, plutonium and the like dissolved in the molten salt 13 are firstly reduced and precipitated on the surface of the liquid Cd cathode 16. Here, as shown in FIG. 2, by rotating the rotation shaft 17, the impeller 18 rotates inside the cylindrical body 19,
As shown by the solid arrow in the figure, the liquid metal as the cathode 16 is
After being sucked up from the lower part of the cylindrical body 19 and flowing out from the upper part of the cylindrical body 19, a downward flow is generated outside the cylindrical body 19. The flow of the liquid metal 16 is performed by depositing a metal such as uranium or plutonium deposited on the upper surface of the liquid Cd cathode 16 by reduction.
Sediment at the bottom to prevent uranium from growing on the surface of the liquid Cd cathode 16.
【００１３】なお、図２ではインペラ１８及び筒体１９
を液体Ｃｄ内部に位置させてウラン、プルトニウム等を
析出させる面積を容器１４の断面積と同じくしたが、図
３に示すように、筒体１９の上部を液体Ｃｄ表面から上
方に突出させて液体Ｃｄを筒体１９の上部から溢れさせ
るようにしてもよい。この場合のウラン、プルトニウム
等を析出させる面積は筒体１９の外径における断面積と
ほぼ同じになり、このように筒体１９の上部を液体Ｃｄ
表面から上方に突出させることによりその析出させる面
積を変化させることができる。In FIG. 2, the impeller 18 and the cylinder 19
Is positioned inside the liquid Cd, and the area for depositing uranium, plutonium, etc. is the same as the cross-sectional area of the container 14. However, as shown in FIG. Cd may overflow from the upper part of the cylinder 19. In this case, the area where uranium, plutonium, etc. are deposited is substantially the same as the cross-sectional area of the outer diameter of the cylinder 19, and thus the upper part of the cylinder 19 is filled with the liquid Cd.
By protruding upward from the surface, the area to be deposited can be changed.
【００１４】また、上述した実施の形態では電解槽１１
下部のＣｄ陽極１２中に使用済の金属燃料を投入した
が、図１の破線で示すように、溶融塩１３中に保持され
るバスケット２１に使用済核燃料を入れて陽極となる電
極２２をバスケット２１に接続しても良い。In the above embodiment, the electrolytic cell 11
Although the spent metal fuel was introduced into the lower Cd anode 12, as shown by the broken line in FIG. 1, the spent nuclear fuel was introduced into the basket 21 held in the molten salt 13, and the electrode 22 serving as the anode was placed in the basket. 21 may be connected.
【００１５】[0015]
【実施例】次に、本発明の実施例を説明する。本発明の
効果を確認するために、図１に示す本発明に係る模擬塩
電解装置１０により水溶液電解を行った。図に示す容器
１４には内径１５０ｍｍ、深さ６０ｍｍのアクリル製の
容器を使用した。電解槽１１内に溶融塩１３の代りに電
解塩水溶液（塩化銀１ｍｏｌ／ｌ）約１０リットルを入
れ、かつ容器１４内にはガリウムを約５００ｃｃを入れ
た後電解を行った。Next, embodiments of the present invention will be described. In order to confirm the effects of the present invention, aqueous solution electrolysis was performed using the simulated salt electrolysis apparatus 10 according to the present invention shown in FIG. As the container 14 shown in the figure, an acrylic container having an inner diameter of 150 mm and a depth of 60 mm was used. About 10 liters of an electrolytic salt aqueous solution (1 mol / l of silver chloride) was placed in the electrolytic bath 11 in place of the molten salt 13, and about 500 cc of gallium was placed in the container 14 and then electrolysis was performed.
【００１６】電解は陽極１２と陰極１６に２０Ａ通電す
ることにより行い、インペラ１８及び筒体１９は図２に
示すように、液体ガリウム内部に位置させて回転軸１７
を回転させることによりガリウム陰極１６を筒体１９の
下部から吸上げて筒体１９の上部から流出させた。筒体
の内径は５０ｍｍであって、撹拌インペラ１８の回転を
上昇させ液体金属が流出することを目視で確認しながら
３時間電解を行った。また、比較のため筒体１９を使用
しない条件でも試験を行った。電解後液体陰極１６を容
器１４ごと取出し、液体陰極１６外への銀デンドライト
の生成状況を確認した。The electrolysis is carried out by applying a current of 20 A to the anode 12 and the cathode 16, and the impeller 18 and the cylinder 19 are positioned inside the liquid gallium and the rotating shaft 17 as shown in FIG.
The gallium cathode 16 was sucked up from the lower part of the cylindrical body 19 by flowing, and was allowed to flow out from the upper part of the cylindrical body 19. The inner diameter of the cylinder was 50 mm, and the rotation of the stirring impeller 18 was increased to perform electrolysis for 3 hours while visually confirming that the liquid metal flowed out. Further, for comparison, a test was performed under the condition where the cylindrical body 19 was not used. After the electrolysis, the liquid cathode 16 was taken out together with the container 14, and the generation state of silver dendrites outside the liquid cathode 16 was confirmed.
【００１７】その結果、筒体１９を用いない場合には、
デンドライドの生成が容器１４表面に認められたが、筒
体１９を使用した場合にはデンドライド状の銀の生成は
筒体１９にはほとんど認められず、また、電解も安定し
て行うことが可能であった。また、試験後液体陰極１６
下部には、筒体１９を用いた場合には銀２３が良好に沈
降していることが確認された。As a result, when the cylindrical body 19 is not used,
Although the generation of dendrites was observed on the surface of the container 14, when the cylinder 19 was used, the generation of dendritic silver was hardly recognized in the cylinder 19, and the electrolysis could be performed stably. Met. After the test, the liquid cathode 16
In the lower part, it was confirmed that silver 23 was successfully settled when the cylindrical body 19 was used.
【００１８】[0018]
【発明の効果】以上述べたように、本発明によれば、容
器に貯留された液体金属に浸漬するように上部より鉛直
下方に延びて設けられた回転軸と、回転軸の下部に取付
けられた液体金属撹拌用のインペラと、インペラを包囲
するように容器内部に設けられた筒体とを備えたので、
回転軸を回転させることによりインペラが液体金属を筒
体の下部から吸上げて筒体の上部から流出させ、筒体の
外側で下方に向う流れを発生させる。この結果、この液
体金属の流れに従って液体金属陰極上面に還元析出した
物質を容器下部に有効に沈降させることができる。ま
た、筒体の上部からウランが析出していない液体金属陰
極を常に流出させるため、液体金属陰極の表面にウラン
が成長することを防止することができ、電解還元による
ウラン、プルトニウム及び超ウラン元素の回収を安定に
行うことができる。As described above, according to the present invention, a rotary shaft extending vertically downward from an upper portion so as to be immersed in liquid metal stored in a container, and a rotary shaft attached to a lower portion of the rotary shaft. Liquid metal stirring impeller, and a cylindrical body provided inside the container so as to surround the impeller,
By rotating the rotating shaft, the impeller sucks up liquid metal from the lower part of the cylindrical body and flows out from the upper part of the cylindrical body to generate a downward flow outside the cylindrical body. As a result, the substance reduced and precipitated on the upper surface of the liquid metal cathode according to the flow of the liquid metal can be effectively settled at the lower portion of the container. In addition, since the liquid metal cathode on which uranium is not precipitated is constantly discharged from the upper part of the cylindrical body, uranium can be prevented from growing on the surface of the liquid metal cathode, and uranium, plutonium, and transuranium elements can be prevented by electrolytic reduction. Can be stably recovered.
【００１９】また、筒体を容器内部で上下動可能に構成
すれば、筒体の上部を液体金属表面から上方に突出させ
て陰極である液体金属の所望の金属を析出させる面積を
変更させることができ、回転軸を容器内部で上下方向に
筒体と連動させれば、筒体を上下動させた場合であって
も液体金属を筒体の下部から有効に吸上げることができ
る。Further, if the cylindrical body is configured to be movable up and down inside the container, the upper part of the cylindrical body is projected upward from the surface of the liquid metal to change the area where the desired metal of the liquid metal serving as the cathode is deposited. If the rotating shaft is vertically linked with the cylinder inside the container, the liquid metal can be effectively sucked from the lower part of the cylinder even when the cylinder is moved up and down.
【図１】本発明の溶融塩電解装置の構成図。FIG. 1 is a configuration diagram of a molten salt electrolysis apparatus of the present invention.
【図２】その装置の容器周囲の拡大断面図。FIG. 2 is an enlarged sectional view around the container of the device.
【図３】その筒体を上昇させた状態を示す図２に対応す
る断面図。FIG. 3 is a sectional view corresponding to FIG. 2 and showing a state in which the cylindrical body is raised.
【図４】従来の溶融塩電解装置を示す断面図。FIG. 4 is a sectional view showing a conventional molten salt electrolysis apparatus.
１０ 溶融塩電解装置 １１ 電解槽 １２ 陽極 １３ 溶融塩 １４ 容器 １６ 陰極（液体金属） １７ 回転軸 １８ インペラ １９ 筒体 DESCRIPTION OF SYMBOLS 10 Molten salt electrolysis apparatus 11 Electrolyzer 12 Anode 13 Molten salt 14 Container 16 Cathode (liquid metal) 17 Rotation axis 18 Impeller 19 Cylindrical body
Claims (3)
通する陽極(12)と、前記使用済核燃料中の少なくともウ
ランを溶解可能な溶融塩(13)と、前記溶融塩中に配置さ
れた容器(14)に貯留された液体金属からなる陰極(16)と
を備え、 溶融塩電解により前記溶融塩(13)中に溶解したウランを
前記液体金属(16)中に析出させるように構成された溶融
塩電解装置において、 前記容器(14)に貯留された液体金属(16)に浸漬するよう
に上部より鉛直下方に延びて設けられた回転軸(17)と、 前記回転軸(17)の下部に取付けられた液体金属撹拌用の
インペラ(18)と、 前記インペラ(18)を包囲するように前記容器(14)内部に
設けられた筒体(19)とを備え、 前記回転軸(17)の回転により前記インペラ(18)が前記液
体金属(16)を前記筒体(19)の下部から吸上げて前記筒体
(19)の上部から流出するように構成されたことを特徴と
する溶融塩電解装置。An electrolytic cell (11) has an anode (12) that communicates with spent nuclear fuel, a molten salt (13) capable of dissolving at least uranium in the spent nuclear fuel, and A cathode (16) made of a liquid metal stored in a container (14) disposed therein, and uranium dissolved in the molten salt (13) is precipitated in the liquid metal (16) by molten salt electrolysis. In the molten salt electrolysis apparatus configured as described above, the rotating shaft (17) provided vertically extending from the upper portion so as to be immersed in the liquid metal (16) stored in the container (14), the rotating shaft ( A liquid metal stirring impeller (18) attached to a lower portion of the container (17); and a cylindrical body (19) provided inside the container (14) so as to surround the impeller (18). The rotation of the shaft (17) causes the impeller (18) to suck up the liquid metal (16) from the lower part of the cylinder (19), and
(19) A molten salt electrolysis apparatus characterized by being configured to flow out from the upper part of (19).
構成された請求項１記載の溶融塩電解装置。2. The molten salt electrolysis apparatus according to claim 1, wherein the tubular body (19) is configured to be vertically movable inside the container (14).
で上下方向に連動可能に構成された請求項１記載の溶融
塩電解装置。3. The molten salt electrolysis apparatus according to claim 1, wherein the cylindrical body (19) and the rotating shaft (17) are configured to be vertically interlockable inside the container (14).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10172297A JP3305227B2 (en) | 1997-04-18 | 1997-04-18 | Molten salt electrolyzer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10172297A JP3305227B2 (en) | 1997-04-18 | 1997-04-18 | Molten salt electrolyzer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH10293193A true JPH10293193A (en) | 1998-11-04 |
| JP3305227B2 JP3305227B2 (en) | 2002-07-22 |
Family
ID=14308203
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10172297A Expired - Fee Related JP3305227B2 (en) | 1997-04-18 | 1997-04-18 | Molten salt electrolyzer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3305227B2 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09257986A (en) * | 1996-03-26 | 1997-10-03 | Toshiba Corp | Molten salt electrolytic refining system |
| JP2008266662A (en) * | 2007-04-16 | 2008-11-06 | Toshiba Corp | Molten salt electrolytic refiner and molten salt electrolytic refining method |
| JP2009133671A (en) * | 2007-11-29 | 2009-06-18 | Toshiba Corp | Method of reprocessing spent fuel |
| KR100945156B1 (en) | 2008-03-31 | 2010-03-08 | 한국원자력연구원 | Molten salt electrorefiner for recovering actinide elements |
| KR100972272B1 (en) | 2009-01-23 | 2010-07-23 | 한국원자력연구원 | Electrowinning apparatus capable of measuring weight of liquid cathode, recovering method of actinide elements and method of monitoring electrodeposit amount of actinide elements |
| KR101598305B1 (en) * | 2014-12-17 | 2016-02-26 | 부산대학교 산학협력단 | High purity metal extraction device and high purity metal extraction method |
-
1997
- 1997-04-18 JP JP10172297A patent/JP3305227B2/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH09257986A (en) * | 1996-03-26 | 1997-10-03 | Toshiba Corp | Molten salt electrolytic refining system |
| JP2008266662A (en) * | 2007-04-16 | 2008-11-06 | Toshiba Corp | Molten salt electrolytic refiner and molten salt electrolytic refining method |
| JP2009133671A (en) * | 2007-11-29 | 2009-06-18 | Toshiba Corp | Method of reprocessing spent fuel |
| KR100945156B1 (en) | 2008-03-31 | 2010-03-08 | 한국원자력연구원 | Molten salt electrorefiner for recovering actinide elements |
| KR100972272B1 (en) | 2009-01-23 | 2010-07-23 | 한국원자력연구원 | Electrowinning apparatus capable of measuring weight of liquid cathode, recovering method of actinide elements and method of monitoring electrodeposit amount of actinide elements |
| KR101598305B1 (en) * | 2014-12-17 | 2016-02-26 | 부산대학교 산학협력단 | High purity metal extraction device and high purity metal extraction method |
Also Published As
| Publication number | Publication date |
|---|---|
| JP3305227B2 (en) | 2002-07-22 |
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