JPH078757A - Isotope separation device - Google Patents
Isotope separation deviceInfo
- Publication number
- JPH078757A JPH078757A JP15945893A JP15945893A JPH078757A JP H078757 A JPH078757 A JP H078757A JP 15945893 A JP15945893 A JP 15945893A JP 15945893 A JP15945893 A JP 15945893A JP H078757 A JPH078757 A JP H078757A
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- Prior art keywords
- product recovery
- product
- electrodes
- vapor flow
- electrode
- Prior art date
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Abstract
(57)【要約】
【目的】所定の濃度の製品を安定的に提供できる同位体
分離装置を提供するものである。
【構成】真空容器1と、この真空容器1内に配置され、
かつ複数種類の同位体を含有する金属原料2を収容する
蒸発用るつぼ3と、上記金属原料2の蒸気流sを発生さ
せる熱源と、発生された蒸気流sの方向に対して平行に
陽電極7と陰電極8とを交互に配置して形成する製品回
収用電極6と、この製品回収用電極6間に流入した蒸気
流s中の特定の同位体を選択的に陽イオン化するレーザ
光10とを備え、上記製品回収用電極間に電圧を印加す
ることによって陽イオン化した特定の同位体を陰電極方
向に偏向させて分離回収する同位体分離装置において、
上記蒸発用るつぼ3と製品回収用電極6との間の蒸気流
中に、製品回収用電極6間へ流入する蒸気流sの流入面
積を調整する手段を設けたことを特徴とする。
(57) [Summary] [Objective] To provide an isotope separation device capable of stably providing a product having a predetermined concentration. [Structure] A vacuum container 1 and the inside of the vacuum container 1,
An evaporation crucible 3 for containing a metal raw material 2 containing a plurality of isotopes, a heat source for generating a vapor stream s of the metal raw material 2, and a positive electrode parallel to the direction of the generated vapor stream s. 7 and the negative electrode 8 are alternately arranged to form a product recovery electrode 6, and a laser beam 10 for selectively cationizing a specific isotope in the vapor stream s flowing between the product recovery electrodes 6. And an isotope separation device for separating and recovering a specific isotope that has been cationized by applying a voltage between the product recovery electrodes, and separating and collecting the specific isotope.
In the vapor flow between the evaporation crucible 3 and the product recovery electrode 6, means for adjusting the inflow area of the vapor flow s flowing between the product recovery electrodes 6 is provided.
Description
【0001】[0001]
【産業上の利用分野】本発明はレーザ光を用いた同位体
分離装置に係わり、特に製品回収用電極間への蒸気流の
流入面積を調整することによって、得られる製品の濃度
を制御することを可能にした同位体分離装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an isotope separation apparatus using a laser beam, and particularly to controlling the concentration of a product obtained by adjusting the inflow area of a vapor flow between electrodes for product recovery. The present invention relates to an isotope separation device that makes it possible.
【0002】[0002]
【従来の技術】レーザ光を用いた同位体分離装置は、例
えば原子炉用燃料を製造するために、天然原料から核反
応を起こす同位体を濃縮する工程等で使用される。2. Description of the Related Art An isotope separation apparatus using a laser beam is used, for example, in a process of concentrating isotopes that cause a nuclear reaction from a natural raw material in order to produce a fuel for a nuclear reactor.
【0003】図7および図8にレーザ光を用いた同位体
分離装置の従来例を示す。真空容器1の底部に、複数種
類の同位体を含有する金属原料2を収容する蒸発用るつ
ぼ3が配置される。この金属原料2には、熱源としての
電子銃4から発射された電子ビーム5が偏向磁場で偏向
されて照射される。金属原料2は加熱溶融されて蒸発
し、蒸気流sを形成する。この蒸気流sの流路上方には
製品回収電極6が配設されている。7 and 8 show a conventional example of an isotope separation device using a laser beam. At the bottom of the vacuum container 1, an evaporation crucible 3 for containing a metal raw material 2 containing plural kinds of isotopes is arranged. The metal raw material 2 is irradiated with an electron beam 5 emitted from an electron gun 4 as a heat source after being deflected by a deflection magnetic field. The metal raw material 2 is heated and melted and evaporated to form a vapor stream s. A product recovery electrode 6 is arranged above the flow path of the vapor flow s.
【0004】この製品回収用電極6の陽電極7と陰電極
8とは、流入する蒸気流sの方向にほぼ平行に対向させ
所要間隔をあけて交互に配設して構成され、陽電極7と
陰電極8間には電界が印加されている。The positive electrode 7 and the negative electrode 8 of the product recovery electrode 6 are arranged so as to face each other substantially parallel to the direction of the inflowing steam flow s and are arranged alternately at a required interval. An electric field is applied between the negative electrode 8 and the negative electrode 8.
【0005】製品回収用電極6の陽電極7と陰電極8間
には、光反応部9が形成される。各光反応部9には蒸気
流sの方向に対してほぼ直角方向(図7においては紙面
に垂直方向)に蒸気流sの中の特定同位体のみを励起、
電離させる波長のレーザ光10がそれぞれ照射される。
このとき、特定の同位体のみが励起され、電離して陽イ
オンとなる。この陽イオンとなった特定の同位体は陰電
極8に吸収され付着し、製品回収器19で回収される。A photoreaction part 9 is formed between the positive electrode 7 and the negative electrode 8 of the product recovery electrode 6. Each photoreactor 9 excites only a specific isotope in the vapor flow s in a direction substantially perpendicular to the direction of the vapor flow s (perpendicular to the paper surface in FIG. 7),
The laser light 10 having a wavelength to be ionized is emitted.
At this time, only specific isotopes are excited and ionized to become positive ions. The specific isotope that has become the cation is absorbed and attached to the negative electrode 8 and collected by the product collector 19.
【0006】一方、レーザ光10の照射によってイオン
化しなかった同位体は、中性原子であり、製品回収用電
極間の電界の影響をほとんど受けることなく、約数%が
製品回収用電極6に付着する程度で電極間を通過して、
二次的に配設された廃品回収用電極11に付着して、回
収される。On the other hand, the isotope that has not been ionized by the irradiation of the laser beam 10 is a neutral atom, and is affected by the electric field between the product recovery electrodes, and about a few percent of the isotope is in the product recovery electrode 6. Passing between the electrodes with the degree of adhesion,
It is attached to and collected by the waste product recovery electrode 11 that is disposed secondarily.
【0007】したがって、陰電極8にはイオン化した同
位体と中性原子とが回収されて製品となる。Accordingly, the negative electrode 8 collects the ionized isotope and the neutral atom, and becomes a product.
【0008】[0008]
【発明が解決しようとする課題】従来の同位体分離装置
において得られる製品濃度は、イオン化した同位体量と
蒸気流から直接付着した中性原子量とで決定される。製
品濃度はレーザパワーを変動させて制御できるが、効率
の良いシステムを提供するためにイオン化率を100%
近くに設定しているので、レーザパワーの変動による制
御だけでは製品濃度を高めることはできず、製品濃度の
低い製品しか製造できない。このため同位体分離装置運
転中に、蒸発用るつぼ内原料の量が変化するなどの原因
で、発生された蒸気流の蒸発分布が変わる等により中性
原子の付着量が変動した場合、所定の濃度の製品が製造
できなかったり、濃度のばらつきが大きい製品が製造さ
れることとなり、所定の濃度の製品を安定的に製造する
ことが困難だった。The product concentration obtained in the conventional isotope separation device is determined by the amount of ionized isotopes and the amount of neutral atoms directly attached from the vapor stream. The product concentration can be controlled by changing the laser power, but the ionization rate is 100% to provide an efficient system.
Since the values are set close to each other, the product concentration cannot be increased only by controlling the fluctuation of the laser power, and only the product having a low product concentration can be manufactured. For this reason, when the amount of attached neutral atoms fluctuates due to changes in the evaporation distribution of the generated vapor flow due to changes in the amount of raw material in the evaporation crucible during operation of the isotope separation device, It has been difficult to stably manufacture a product having a predetermined concentration because a product having a concentration cannot be manufactured or a product having a large variation in concentration is manufactured.
【0009】本発明は上述した事情を考慮してなされた
もので、製品回収用電極間に流入する蒸気流の流入面積
を調整できる手段を設けたことによって、所定の濃度の
製品を安定的に提供できる同位体分離装置を提供するこ
とを目的とする。The present invention has been made in consideration of the above-mentioned circumstances. By providing means for adjusting the inflow area of the vapor flow flowing between the product recovery electrodes, the product having a predetermined concentration can be stably stabilized. It is an object to provide an isotope separation device that can be provided.
【0010】[0010]
【課題を解決するための手段】上記目的を達成するため
本発明に係る同位体分離装置は、請求項1に記載したよ
うに、真空容器と、この真空容器内に配置され、かつ複
数種類の同位体を含有する金属原料を収容する蒸発用る
つぼと、上記金属原料の蒸気流を発生させる熱源と、発
生された蒸気流の方向に対して平行に陽電極と陰電極と
を交互に配置して形成する製品回収用電極と、この製品
回収用電極間に流入した蒸気流にレーザ光を照射して特
定の同位体を選択的に陽イオン化させるレーザ光発射装
置とを備え、上記製品回収用電極間に電圧を印加するこ
とによって陽イオン化した特定の同位体を陰電極方向に
偏向させて分離回収する同位体分離装置において、上記
蒸発用るつぼと製品回収用電極との間の蒸気流中に、製
品回収用電極間へ流入する蒸気の流入面積を調整する手
段を設けたものである。In order to achieve the above object, an isotope separation apparatus according to the present invention has a vacuum container and a plurality of kinds of vacuum containers arranged in the vacuum container as described in claim 1. An evaporation crucible containing a metal raw material containing an isotope, a heat source for generating a vapor flow of the metal raw material, and a positive electrode and a negative electrode are arranged alternately in parallel to the direction of the generated vapor flow. And a laser beam emitting device for irradiating the vapor stream flowing between the product collecting electrodes with a laser beam to selectively positively ionize a specific isotope. In an isotope separation device that separates and recovers specific cationized isotopes by applying a voltage between the electrodes in the direction of the negative electrode, the isotope separation device collects a vapor flow between the evaporation crucible and the product recovery electrode , Between electrodes for product recovery It is provided with a means for adjusting the flow area of the vapor inlet.
【0011】[0011]
【作用】本発明によれば、上記金属原料から発生される
蒸気流の製品回収用電極間へ流入する蒸気流の流入面積
を調整することにより、製品回収用電極に付着される中
性原子量が可変となる。すなわち、蒸気流の製品回収用
電極間における流入面積を減少させると蒸気流と製品回
収用電極との隙間が広がり、製品回収用電極に付着する
中性原子量が減少する。また、蒸気流の製品回収用電極
間における流入面積を増大させると、蒸気流と製品回収
用電極との隙間が狭まり、製品回収用電極に付着する中
性原子量が増加する。製品濃度は製品に含まれる中性原
子の量に依存するので、蒸気流の製品回収用電極間の流
入面積を制御することによって製品濃度が制御できる。According to the present invention, the amount of neutral atoms attached to the product recovery electrodes is adjusted by adjusting the inflow area of the steam flow generated between the product recovery electrodes of the steam flow generated from the metal raw material. It is variable. That is, when the inflow area between the product recovery electrodes of the vapor flow is reduced, the gap between the vapor flow and the product recovery electrode is widened, and the amount of neutral atoms attached to the product recovery electrode is reduced. Further, when the inflow area of the vapor recovery between the product recovery electrodes is increased, the gap between the vapor flow and the product recovery electrode is narrowed, and the amount of neutral atoms attached to the product recovery electrode is increased. Since the product concentration depends on the amount of neutral atoms contained in the product, the product concentration can be controlled by controlling the inflow area of the vapor flow between the product recovery electrodes.
【0012】[0012]
【実施例】以下、本発明に係る同位体分離装置の実施例
について、添付図面を参照して説明する。なお既に説明
した従来例と同一部分には同符号を付して、詳細な説明
は省略する。EXAMPLES Examples of the isotope separation apparatus according to the present invention will be described below with reference to the accompanying drawings. The same parts as those of the conventional example described above are designated by the same reference numerals, and detailed description thereof will be omitted.
【0013】図1は本発明の第1実施例を表す断面図で
ある。図1において、真空容器1の底部に、複数種類の
同位体を含有する金属原料2を収容する蒸発用るつぼ3
が配置される。この金属原料2には、熱源としての電子
銃4から発射された電子ビーム5が偏向磁場で偏向され
て照射される。金属原料2は加熱溶融されて蒸発し、蒸
気流sを形成する。この蒸気流sの流路上方には製品回
収用電極6が配設されている。FIG. 1 is a sectional view showing a first embodiment of the present invention. In FIG. 1, an evaporation crucible 3 for accommodating a metal raw material 2 containing a plurality of types of isotopes is provided at the bottom of a vacuum container 1.
Are placed. This metal raw material 2 is irradiated with an electron beam 5 emitted from an electron gun 4 as a heat source after being deflected by a deflection magnetic field. The metal raw material 2 is heated and melted and evaporated to form a vapor stream s. A product recovery electrode 6 is provided above the flow path of the vapor flow s.
【0014】蒸気流sと製品回収用電極6との間に、製
品回収用電極6間へ流入する蒸気流sの流入面積を調整
する手段としての蒸気整流器12が設けられている。こ
の蒸気整流器12には蒸気の流れを制御する手段である
蒸気整流板13が取り付けられている。同位体濃度測定
器14によって製品の濃度をモニタし、所定の製品濃度
となるように蒸気整流器制御装置15によって、蒸気整
流器12が制御され、蒸気流入面積が調整される。A steam rectifier 12 is provided between the steam flow s and the product recovery electrode 6 as a means for adjusting the inflow area of the steam flow s flowing between the product recovery electrodes 6. The steam rectifier 12 is provided with a steam rectifying plate 13, which is means for controlling the flow of steam. The concentration of the product is monitored by the isotope concentration measuring device 14, and the steam rectifier 12 is controlled by the steam rectifier control device 15 so that the predetermined product concentration is obtained, and the steam inflow area is adjusted.
【0015】製品回収用電極6の陽電極7と陰電極8間
には、光反応部9が形成され、各光反応部9には蒸気流
sの方向に対してほぼ直角方向に、レーザ装置から発射
されるレーザ光10がそれぞれ照射され、特定の同位体
のみが励起され、電離して陽イオンとなり、製品回収用
電極6の陰電極に吸収され付着し、製品回収器19で回
収される。イオン化しなかった同位体はごく少量の一部
が製品回収用電極6に付着し、残りは廃品回収用電極1
1に付着して回収される。A photoreaction part 9 is formed between the positive electrode 7 and the negative electrode 8 of the product recovery electrode 6, and each photoreaction part 9 is provided with a laser device in a direction substantially perpendicular to the direction of the vapor flow s. Each of the laser beams 10 emitted from the product is irradiated, and only a specific isotope is excited and ionized into positive ions, which are absorbed and attached to the negative electrode of the product recovery electrode 6 and recovered by the product recovery device 19. . A small amount of the non-ionized isotope adheres to the product recovery electrode 6, and the rest is the waste product recovery electrode 1.
1 is attached and collected.
【0016】次に、本実施例の作用について説明する。Next, the operation of this embodiment will be described.
【0017】本実施例の同位体分離装置において、金属
原料2が加熱され発生した蒸気流sは、蒸気整流器12
によって一部が遮断される。In the isotope separation apparatus of this embodiment, the steam flow s generated by heating the metal raw material 2 is the steam rectifier 12
Is partially blocked by.
【0018】一方、同位体濃度測定器14によって製品
回収器19で回収された製品の濃度をモニタして、所定
の濃度が得られるように蒸気整流器制御装置15によっ
て蒸気整流器12中の蒸気整流板13を可動させる。On the other hand, the isotope concentration measuring device 14 monitors the concentration of the product recovered by the product recovering device 19, and the steam rectifier controller 15 controls the steam rectifying plate in the steam rectifier 12 so that a predetermined concentration can be obtained. Move 13
【0019】このときの、製品回収電極6および蒸気整
流器12を図2に示す。蒸気整流板13が蒸気整流板角
度θを変化させながら可動し、蒸気流遮断領域16(斜
線部)を変化させ蒸気流の流入面積を変化させる。この
蒸気流の流入面積の変化により、中性原子の付着率が変
化して製品の濃度が制御できる。FIG. 2 shows the product recovery electrode 6 and the vapor rectifier 12 at this time. The steam straightening plate 13 moves while changing the steam straightening plate angle θ, and changes the steam flow blocking region 16 (hatched portion) to change the inflow area of the steam flow. Due to the change of the inflow area of the vapor flow, the attachment rate of neutral atoms changes, and the concentration of the product can be controlled.
【0020】この蒸気整流器12の制御量と中性原子の
付着率および製品濃度との関係を図3に示す。製品回収
電極7間の蒸気流sの流入面積が最小となるように、上
記θの角度を設定すると中性原子付着率が低下して製品
濃度が増加する。FIG. 3 shows the relationship between the control amount of the steam rectifier 12, the attachment rate of neutral atoms, and the product concentration. When the angle of θ is set so that the inflow area of the vapor flow s between the product recovery electrodes 7 is minimized, the neutral atom attachment rate decreases and the product concentration increases.
【0021】また、上記θの角度を変化させて蒸気流s
の流入面積を大きくしていくと、中性原子の付着率が増
加して製品濃度が低下する。Further, by changing the angle of θ, the steam flow s
When the inflow area of is increased, the attachment rate of neutral atoms increases and the product concentration decreases.
【0022】したがって、金属原料2から発生される蒸
気流の、製品回収用電極6間における流入面積を調整す
ることによって中性原子の付着量を制御することがで
き、同位体分離装置運転中にるつぼ内原料の量が変化す
るなどの原因で、発生された蒸気流の蒸発分布が変わる
等により中性原子の付着量が変動した場合においても、
所定の濃度の製品を安定的に製造することができる。Therefore, the amount of attachment of neutral atoms can be controlled by adjusting the inflow area of the vapor flow generated from the metal raw material 2 between the product recovery electrodes 6, and during the operation of the isotope separation device. Even if the amount of attached neutral atoms changes due to changes in the evaporation distribution of the generated vapor flow due to changes in the amount of raw material in the crucible, etc.
It is possible to stably manufacture a product having a predetermined concentration.
【0023】図4に本発明の第2実施例を示す。第2実
施例は第1実施例における蒸気整流器12の蒸気整流板
13の構成が異なるのみなのでその他の説明は省略し
た。FIG. 4 shows a second embodiment of the present invention. The second embodiment is different from the first embodiment only in the configuration of the steam rectifying plate 13 of the steam rectifier 12, and therefore the other description is omitted.
【0024】蒸気整流板が13a、13bの2枚で構成
されており、この蒸気整流板13a、13bを独立に制
御することができるので、製品回収用電極6の各面6
a、6bの中性原子の付着量を独立に変化させることが
可能になる。その他の構成、作用、効果は実施例1と同
一であり、同一符号を用いて説明は省略する。Since the steam rectifying plates 13a and 13b are composed of two sheets, and the steam rectifying plates 13a and 13b can be independently controlled, each surface 6 of the product collecting electrode 6 can be controlled.
It becomes possible to independently change the attachment amounts of the neutral atoms of a and 6b. Other configurations, operations, and effects are the same as those of the first embodiment, and the same reference numerals are used and the description thereof is omitted.
【0025】図5に本発明の第3実施例を示す。第3実
施例は第1実施例に示された同位体分離装置に、レーザ
パワー制御装置17を追加して、レーザ光発生装置18
から出射されるレーザ光のレーザパワーも制御可能にし
た。図6に蒸気整流器12の制御量と中性原子の付着率
および製品濃度との関係を示す。レーザパワー変動させ
ることによって、図中の斜線部に示す範囲で製品の濃度
を変化させることが可能となる。その他の構成、作用、
効果は第1実施例と同一である。FIG. 5 shows a third embodiment of the present invention. In the third embodiment, a laser power control device 17 is added to the isotope separation device shown in the first embodiment, and a laser light generator 18 is added.
The laser power of the laser light emitted from is also controllable. FIG. 6 shows the relationship between the control amount of the steam rectifier 12, the attachment rate of neutral atoms, and the product concentration. By varying the laser power, it is possible to change the density of the product within the range shown by the shaded area in the figure. Other configurations, functions,
The effect is the same as that of the first embodiment.
【0026】[0026]
【発明の効果】以上述べたように本発明に係る同位体分
離装置によれば、同位体分離装置運転中に、るつぼ内原
料の量が変化するなどの原因で、発生された蒸気流の蒸
発分布が変わる等により中性原子の付着量が変動した場
合においても、製品回収電極間へ流入する蒸気の流入面
積を流入面積調整手段にて調整することによって、上記
製品回収用電極に付着する中性原子量が制御でき、その
結果、製品濃度が制御できるので、所定の濃度の製品を
安定的に提供できるといった効果がある。As described above, according to the isotope separation device of the present invention, vaporization of the vapor stream generated due to a change in the amount of the raw material in the crucible during the operation of the isotope separation device is performed. Even when the amount of attached neutral atoms fluctuates due to changes in distribution, etc., by adjusting the inflow area adjusting means for the inflow area of the vapor flowing between the product recovery electrodes, Since the atomic weight of the organic compound can be controlled, and as a result, the product concentration can be controlled, there is an effect that a product having a predetermined concentration can be stably provided.
【図1】本発明に係る同位体分離装置の第1実施例を示
す断面図。FIG. 1 is a sectional view showing a first embodiment of an isotope separation device according to the present invention.
【図2】本発明に係る同位体分離装置の第1実施例にお
ける、製品回収用電極と蒸気整流器およびその周辺の蒸
気流とを示す図。FIG. 2 is a diagram showing a product recovery electrode, a vapor rectifier and a vapor flow around the same in the first embodiment of the isotope separation device according to the present invention.
【図3】本発明に係る同位体分離装置の第1実施例にお
ける、蒸気整流器の制御量と中性原子の付着率および製
品濃度との関係を表す図。FIG. 3 is a diagram showing the relationship between the control amount of the vapor rectifier, the attachment rate of neutral atoms, and the product concentration in the first embodiment of the isotope separation device according to the present invention.
【図4】本発明に係る同位体分離装置の第2実施例にお
ける、製品回収用電極と蒸気整流器およびその周辺の蒸
気流とを示す図。FIG. 4 is a diagram showing a product recovery electrode, a vapor rectifier and a vapor flow around the same in a second embodiment of the isotope separation device according to the present invention.
【図5】本発明に係る同位体分離装置の第3実施例を示
す、図1におけるV−V矢視断面図。5 is a sectional view taken along the line VV in FIG. 1, showing a third embodiment of the isotope separation device according to the present invention.
【図6】本発明に係る同位体分離装置の第3実施例にお
ける、蒸気整流器の制御量と中性原子の付着率および製
品濃度との関係を表す図。FIG. 6 is a diagram showing the relationship between the control amount of the vapor rectifier, the attachment rate of neutral atoms and the product concentration in the third embodiment of the isotope separation device according to the present invention.
【図7】従来の同位体分離装置の構成を示す断面図。FIG. 7 is a cross-sectional view showing the configuration of a conventional isotope separation device.
【図8】図7におけるVIII−VIII矢視断面図。8 is a sectional view taken along the line VIII-VIII in FIG.
1 真空容器 2 金属原料 3 蒸発用るつぼ 4 電子銃 5 電子ビーム 6 製品回収用電極 6a 製品回収用電極面 6b 製品回収用電極面 7 陽電極 8 陰電極 9 光反応部 10 レーザ光 11 廃品回収用電極 12 蒸気整流器 13,13a,13b 蒸気整流板 14 同位体濃度測定器 15 蒸気整流器制御装置 16 蒸気流遮断領域 17 レーザパワー制御装置 18 レーザ光発生装置 19 製品回収器 1 Vacuum Container 2 Metallic Material 3 Evaporating Crucible 4 Electron Gun 5 Electron Beam 6 Product Recovery Electrode 6a Product Recovery Electrode Surface 6b Product Recovery Electrode Surface 7 Positive Electrode 8 Negative Electrode 9 Photoreactive Part 10 Laser Light 11 Waste Product Recovery Electrode 12 Steam rectifier 13, 13a, 13b Steam rectifier 14 Isotope concentration measuring instrument 15 Steam rectifier controller 16 Steam flow blocking area 17 Laser power controller 18 Laser light generator 19 Product collector
Claims (1)
れ、かつ複数種類の同位体を含有する金属原料を収容す
る蒸発用るつぼと、上記金属原料の蒸気流を発生させる
熱源と、発生された蒸気流の方向に対して平行に陽電極
と陰電極とを交互に配置して形成する製品回収用電極
と、この製品回収用電極間に流入した蒸気流にレーザ光
を照射して特定の同位体を選択的に陽イオン化させるレ
ーザ光発射装置とを備え、上記製品回収用電極間に電圧
を印加することによって陽イオン化した特定の同位体を
陰電極方向に偏向させて分離回収する同位体分離装置に
おいて、上記蒸発用るつぼと製品回収用電極との間の蒸
気流中に、製品回収用電極間へ流入する蒸気流の流入面
積を調整する手段を設けたことを特徴とする同位体分離
装置。1. A vacuum container, an evaporation crucible which is arranged in the vacuum container and which contains a metal raw material containing plural kinds of isotopes, and a heat source which generates a vapor flow of the metal raw material. The product recovery electrodes formed by alternately arranging the positive electrodes and the negative electrodes in parallel to the direction of the vapor flow, and the vapor flow flowing between the product recovery electrodes are irradiated with laser light to obtain a specific A laser beam emitting device for selectively cationizing isotopes, and by applying a voltage between the product recovery electrodes, the specific cationized isotopes are deflected toward the negative electrode and separated and recovered. In the separation device, a means for adjusting the inflow area of the vapor flow flowing between the product recovery electrodes in the vapor flow between the evaporation crucible and the product recovery electrode is provided. apparatus.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15945893A JP3263189B2 (en) | 1993-06-29 | 1993-06-29 | Isotope separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15945893A JP3263189B2 (en) | 1993-06-29 | 1993-06-29 | Isotope separation device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH078757A true JPH078757A (en) | 1995-01-13 |
| JP3263189B2 JP3263189B2 (en) | 2002-03-04 |
Family
ID=15694208
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15945893A Expired - Fee Related JP3263189B2 (en) | 1993-06-29 | 1993-06-29 | Isotope separation device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3263189B2 (en) |
-
1993
- 1993-06-29 JP JP15945893A patent/JP3263189B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JP3263189B2 (en) | 2002-03-04 |
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