JPH11290606A - Multi-stage centrifugal extractor - Google Patents

Multi-stage centrifugal extractor

Info

Publication number
JPH11290606A
JPH11290606A JP9614798A JP9614798A JPH11290606A JP H11290606 A JPH11290606 A JP H11290606A JP 9614798 A JP9614798 A JP 9614798A JP 9614798 A JP9614798 A JP 9614798A JP H11290606 A JPH11290606 A JP H11290606A
Authority
JP
Japan
Prior art keywords
density liquid
extraction means
centrifugal
supply chamber
rotary drum
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP9614798A
Other languages
Japanese (ja)
Inventor
Kazuhiro Arai
和浩 荒井
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP9614798A priority Critical patent/JPH11290606A/en
Publication of JPH11290606A publication Critical patent/JPH11290606A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/30Nuclear fission reactors
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies

Landscapes

  • Extraction Or Liquid Replacement (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a multi-stage centrifugal extractor designed for efficient transfer of substance between two liquids of different densities. SOLUTION: In centrifugal extracting means A, B, C, D, E, F, a radioactive substance contained in a dissolved salt entering an inlet channel, 28 to move through the individual centrifugal extracting means A, B, C, D, E, F and transfer passages 29 therebetween toward an outlet channel 30 travels to a molten metal entering an inlet channel 31 to move through the individual centrifugal extracting means F, E, D, C, B, A and transfer passages 32 therebetween toward an outlet channel 33, thus effecting efficient removal of the radioactive substance contained in the dissolved salt.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は多段遠心抽出器に関
するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a multistage centrifugal extractor.

【0002】[0002]

【従来の技術】原子炉から取り出された使用済み燃料の
乾式再処理作業には、使用済み燃料を溶融塩(LiCl
−KCl)を用いて電解精製することにより生じた放射
性物質溶融廃塩に、カドミウム(Cd)系などの溶融金
属を混合して、放射性物質溶融廃塩の放射性物質(TR
U)を溶融金属側へ移行させ、溶融塩と溶融金属とを分
離した後、放射性物質が取り除かれた溶融塩を、再び使
用済み燃料の電解精製に用いることを繰り返し行う放射
性物質抽出工程がある。
2. Description of the Related Art For dry reprocessing of spent fuel taken out of a nuclear reactor, spent fuel is subjected to molten salt (LiCl
-KCl) is mixed with a molten metal such as cadmium (Cd) based on the molten waste radioactive salt generated by electrolytic purification using the radioactive substance (TR
U) is transferred to the molten metal side, and after separating the molten salt and the molten metal, there is a radioactive substance extraction step of repeatedly using the molten salt from which the radioactive substance has been removed for the electrolytic purification of the spent fuel again. .

【0003】図7は上述した放射性物質抽出工程におけ
る溶融塩と溶融金属との分離手段として近年提案されて
いる遠心抽出器の一例である。
FIG. 7 shows an example of a centrifugal extractor recently proposed as a means for separating molten salt and molten metal in the above-mentioned radioactive substance extraction step.

【0004】この遠心抽出器は、底部中央に上下方向へ
貫通する導入孔1が穿設され且つ上端寄り部分に周方向
へ貫通する複数の流出孔2が穿設された略円筒状の回転
胴3と、該回転胴3の下側寄り部分を周方向に取り囲む
供給室4及び回転胴3の上側寄り部分を周方向に取り囲
み且つ回転胴3寄り部分が開口した上下2段の液体溜め
18,17を有するケーシング9と、前記の回転胴3を
一方向に回転させる駆動装置10とを備えている。
This centrifugal extractor has a substantially cylindrical rotating body having an inlet hole 1 penetrating vertically in the center of the bottom and a plurality of outlet holes 2 penetrating in the circumferential direction in a portion near the upper end. A supply chamber 4 surrounding the lower portion of the rotary drum 3 in the circumferential direction; and a liquid reservoir 18 of two upper and lower stages surrounding the upper portion of the rotary drum 3 in the circumferential direction and having an open portion near the rotary drum 3. And a drive device 10 for rotating the rotary drum 3 in one direction.

【0005】ケーシング9の下端寄り部分には、放射性
物質を含んだ溶融塩5を供給室4へ流入させ得る溶融塩
供給口6と、溶融塩5から放射性物質を取り除くための
溶融金属7を供給室4へ流入させ得る溶融金属供給口8
とが、横向きに穿設されている。
A molten salt supply port 6 through which a molten salt 5 containing a radioactive substance can flow into a supply chamber 4 and a molten metal 7 for removing the radioactive substance from the molten salt 5 are supplied to a portion near the lower end of the casing 9. Molten metal supply port 8 that can flow into chamber 4
Are pierced sideways.

【0006】また、ケーシング9内の上下方向中間部に
は、回転胴3を周方向に取り囲み且つ回転胴3の外周面
に対して微小間隙を隔てて対峙する突起部16が形成さ
れている。
[0006] A projection 16 is formed at an intermediate portion in the vertical direction in the casing 9 so as to surround the rotary drum 3 in the circumferential direction and to face the outer peripheral surface of the rotary drum 3 with a small gap therebetween.

【0007】溶融塩供給口6へ送給される溶融塩5及び
溶融金属供給口8へ送給される溶融金属7は、供給室4
から導入孔1を経て回転胴3の内部へ流入する。
The molten salt 5 supplied to the molten salt supply port 6 and the molten metal 7 supplied to the molten metal supply port 8 are supplied to the supply chamber 4.
Through the introduction hole 1 to flow into the inside of the rotary drum 3.

【0008】このとき、回転胴3が一方向へ連続的に回
転していると、回転胴3の回転に伴う遠心力の影響、並
びに溶融塩5と溶融金属7との密度差によって、回転胴
3の内側面に沿って液位が上昇する溶融金属7の環状の
液層と、当該液層の内側面に沿って液位が上昇する溶融
塩5の環状の液層とが形成されることになる。
At this time, when the rotating drum 3 is continuously rotating in one direction, the rotating drum 3 is affected by the centrifugal force accompanying the rotation of the rotating drum 3 and the density difference between the molten salt 5 and the molten metal 7. Forming an annular liquid layer of molten metal 7 whose liquid level rises along the inner surface of 3 and an annular liquid layer of molten salt 5 whose liquid level rises along the inner surface of the liquid layer become.

【0009】回転胴3の上端には、回転胴3の回転に伴
って液位が上昇する溶融金属7を、回転胴3の外部へ導
き得る環状の外側堰11が回転胴3に対して同軸に設け
られている。
At the upper end of the rotating drum 3, an annular outer weir 11 for guiding the molten metal 7 whose liquid level rises with the rotation of the rotating drum 3 to the outside of the rotating drum 3 is coaxial with the rotating drum 3. It is provided in.

【0010】回転胴3の上端近傍部分には、前記の外側
堰11の下方に位置し且つ回転胴3の回転に伴って液位
が上昇する溶融塩5を、流出孔2から回転胴3の外部へ
導き得る中空円盤状の内側堰12が回転胴3に対して同
軸に設けられている。
In the vicinity of the upper end of the rotating drum 3, a molten salt 5, which is located below the outer weir 11 and whose liquid level rises with the rotation of the rotating drum 3, is discharged from the outlet hole 2 into the rotating drum 3. A hollow disk-shaped inner weir 12 that can be guided to the outside is provided coaxially with the rotating drum 3.

【0011】この内側堰12の外縁部には、回転胴3の
内方に位置して上下方向に貫通する複数の流通孔13
が、周方向に間隔を隔てて穿設されており、回転胴3の
回転に伴って液位が上昇する溶融金属7は、上記の流通
孔13を経て外側堰11に到達するようになっている。
In the outer edge of the inner weir 12, there are provided a plurality of flow holes 13 which are located inside the rotary drum 3 and penetrate vertically.
However, the molten metal 7, which is drilled at intervals in the circumferential direction and whose liquid level rises with the rotation of the rotary drum 3, reaches the outer weir 11 through the above-described flow hole 13. I have.

【0012】また、内側堰12の底部中央には、回転胴
3の回転に伴い液位が上昇する溶融塩5を、流出孔2へ
導くための開口14が形成されている。
An opening 14 is formed at the center of the bottom of the inner weir 12 to guide the molten salt 5 whose liquid level rises with the rotation of the rotary drum 3 to the outflow hole 2.

【0013】更に、内側堰12には、ケーシング9の上
部外方に設置された駆動装置10からケーシング9の上
部及び内側堰12を貫通して下方へ延びる駆動軸15が
連結されており、駆動装置10の回転力が、駆動軸15
及び内側堰12を介して回転胴3に伝達されるようにな
っている。
Further, a drive shaft 15 is connected to the inner weir 12 and extends downward from the drive unit 10 installed outside the upper part of the casing 9 through the upper part of the casing 9 and the inner weir 12. The rotational force of the device 10 is
And transmitted to the rotating drum 3 via the inner weir 12.

【0014】下側の液体溜め17は、流出孔2の穿設位
置上縁から径方向外方へ向って下り勾配をなす傾斜面1
9を有し、上側の液体溜め18は、外側堰11の上方か
ら径方向外方へ向って下り勾配をなす傾斜面20を有し
ている。
The lower liquid reservoir 17 is formed on the inclined surface 1 having a downward gradient from the upper edge of the outflow hole 2 to the outside in the radial direction.
9, and the upper liquid reservoir 18 has an inclined surface 20 that slopes downward from the upper part of the outer weir 11 radially outward.

【0015】内側堰12を経て回転胴3の外部へ飛散す
る溶融塩5や外側堰11を経て回転胴3の外部へ飛散す
る溶融金属7は、上記の傾斜面19,20に衝突して、
液体溜め17,18に捕捉されることになる。
The molten salt 5 scattered to the outside of the rotating drum 3 via the inner weir 12 and the molten metal 7 scattered to the outside of the rotating drum 3 via the outer weir 11 collide with the above-mentioned inclined surfaces 19 and 20,
The liquid will be trapped in the liquid reservoirs 17 and 18.

【0016】液体溜め17に捕捉された溶融塩5は、ケ
ーシング9の上端寄り部分に横向きに穿設された溶融塩
排出口21から外部へ流出するように、液体溜め18に
捕捉された溶融金属7は、ケーシング9の上端寄り部分
に横向きに穿設された溶融金属排出口22から外部へ流
出するようになっている。
The molten salt 5 trapped in the liquid reservoir 17 flows out of the molten salt discharge port 21 formed in the portion near the upper end of the casing 9 to the outside. Numeral 7 flows to the outside from a molten metal discharge port 22 formed in the casing 9 near the upper end in a lateral direction.

【0017】更に、供給室4の内底部には、該供給室4
から回転胴3の内部への溶融塩5及び溶融金属7の流入
が、回転胴3の回転に伴って促進されるように、複数の
導入促進翼23が放射状に設けられ、駆動軸15の下端
部には、供給室4から回転胴3の内側面へ向って溶融塩
5及び溶融金属7を流入させるための円盤状の偏向板2
4が、導入孔1に正対し且つ回転胴3の内底部近傍に位
置するように取り付けられている。
Further, the supply chamber 4 is provided at the inner bottom of the supply chamber 4.
A plurality of introduction promoting wings 23 are radially provided so that the inflow of the molten salt 5 and the molten metal 7 from inside to the inside of the rotary drum 3 is promoted with the rotation of the rotary drum 3, and the lower end of the drive shaft 15 is provided. The disk-shaped deflecting plate 2 for allowing the molten salt 5 and the molten metal 7 to flow from the supply chamber 4 toward the inner surface of the rotary drum 3
4 is attached so as to face the introduction hole 1 and to be located near the inner bottom of the rotating drum 3.

【0018】図7に示す遠心抽出器を用いて溶融塩5か
ら放射性物質を取り除く際には、駆動装置10により回
転胴3を一方向へ連続的に回転させ、放射性物質を含ん
でいる溶融塩5を、溶融塩供給口6から供給室4へ流入
させるとともに、放射性物質を取り込み得る溶融金属7
を、溶融金属供給口8から供給室4へ流入させる。
When the radioactive material is removed from the molten salt 5 using the centrifugal extractor shown in FIG. 7, the rotary unit 3 is continuously rotated in one direction by the driving device 10 and the molten salt containing the radioactive material is removed. 5 flows into the supply chamber 4 from the molten salt supply port 6 and a molten metal 7 capable of taking in radioactive substances.
From the molten metal supply port 8 into the supply chamber 4.

【0019】供給室4に流入した溶融塩5及び溶融金属
7は、回転胴3の回転に伴い混合されながら、供給室4
の底部から導入孔1を経て回転胴3の内部へ流入する。
The molten salt 5 and the molten metal 7 flowing into the supply chamber 4 are mixed with the rotation of the rotary drum 3 while
From the bottom through the introduction hole 1 into the rotary drum 3.

【0020】このとき、溶融塩5に含まれている放射性
物質が溶融金属7へ移行し、溶融塩5から放射性物質が
取り除かれる。
At this time, the radioactive substance contained in the molten salt 5 moves to the molten metal 7, and the radioactive substance is removed from the molten salt 5.

【0021】放射性物質を取り込んだ溶融金属7は、回
転胴3の内部、外側堰11、液体溜め18を経て、溶融
金属排出口22からケーシング9の外部へ流出し、放射
性物質が取り除かれた溶融塩5は、回転胴3の内部、内
側堰12、液体溜め17を経て、溶融塩排出口21から
ケーシング9の外部へ流出する。
The molten metal 7 containing the radioactive material flows through the inside of the rotary drum 3, the outer weir 11, and the liquid reservoir 18, flows out of the molten metal outlet 22 to the outside of the casing 9, and the molten metal from which the radioactive material has been removed is removed. The salt 5 flows out of the casing 9 from the molten salt discharge port 21 through the inside of the rotary drum 3, the inner weir 12, and the liquid reservoir 17.

【0022】[0022]

【発明が解決しようとする課題】しかしながら、溶融塩
5と溶融金属7との分離作業の効率向上を図るために、
回転胴3を高回転数で駆動すると、回転胴3の外周面と
供給室4の内周面との間に介在している溶融塩5及び溶
融金属7の混合液体に、回転胴3の回転に起因する遠心
力が作用して液位上昇が生じる。
However, in order to improve the efficiency of the work of separating the molten salt 5 and the molten metal 7,
When the rotating drum 3 is driven at a high rotation speed, the liquid mixture of the molten salt 5 and the molten metal 7 interposed between the outer peripheral surface of the rotating drum 3 and the inner peripheral surface of the supply chamber 4 is rotated. The liquid level rises due to the centrifugal force caused by the pressure.

【0023】これにより、未分離の溶融塩5及び溶融金
属7の混合液体が、回転胴3の外周面とケーシング9の
突起部16の内周面との間の間隙から上方へ漏洩して液
体溜め17に流入することになる。
As a result, the liquid mixture of the unseparated molten salt 5 and the molten metal 7 leaks upward from the gap between the outer peripheral surface of the rotary drum 3 and the inner peripheral surface of the projection 16 of the casing 9 to be liquid. It will flow into the reservoir 17.

【0024】すなわち、図7に示す遠心抽出器では、単
に回転胴3の回転数を高くしただけでは、溶融塩5から
溶融金属7への放射性物質の移行の効率向上を図ること
ができない。
That is, in the centrifugal extractor shown in FIG. 7, it is not possible to improve the efficiency of the transfer of the radioactive substance from the molten salt 5 to the molten metal 7 simply by increasing the rotation speed of the rotating drum 3.

【0025】本発明は上述した実情に鑑みてなしたもの
で、密度の異なる2種類の液体間における物質の移行を
効率よく行える多段遠心抽出器を提供することを目的と
している。
The present invention has been made in view of the above circumstances, and has as its object to provide a multistage centrifugal extractor capable of efficiently transferring a substance between two types of liquids having different densities.

【0026】[0026]

【課題を解決するための手段】上記目的を達成するため
本発明の多段遠心抽出器では、底部中央に上下方向へ貫
通する導入孔が穿設され且つ上端寄り部分に周方向へ貫
通する流出孔が穿設された略円筒状の回転胴と、回転胴
の下側寄り部分を周方向に取り囲む供給室と、回転胴の
上側寄り部分を周方向に取り囲み且つ回転胴寄り部分が
開口した低密度液体溜め及び高密度液体溜めと、回転胴
の上端に設けられ且つ供給室から導入孔を経て回転胴内
に流入する高密度液体を回転胴の回転に伴う遠心力によ
り高密度液体溜めへ導き得る外側堰と、該外側堰の下方
に位置するように回転胴の上端近傍部分に設けられ且つ
供給室から導入孔を経て回転胴内に流入する低密度液体
を回転胴の回転に伴う遠心力により流出孔を介して低密
度流体溜めへ導き得る内側堰とをそれぞれ有する複数の
遠心抽出手段が横方向に一列に配置され、最前端に位置
する遠心抽出手段の供給室へ外部から連通する低密度液
体入口流路と、各遠心抽出手段間に位置し且つ前方側に
位置する遠心抽出手段の低密度液体溜めから後方側に位
置する遠心抽出手段の供給室へ連通する低密度液体移送
流路と、最後端に位置する遠心抽出手段の低密度液体溜
めから外部へ連通する低密度液体出口流路と、最後端に
位置する遠心抽出手段の供給室へ外部から連通する高密
度液体入口流路と、各遠心抽出手段間に位置し且つ後方
側に位置する遠心抽出手段の高密度液体溜めから前方側
に位置する遠心抽出手段の供給室へ連通する高密度液体
移送流路と、最前端に位置する遠心抽出手段の高密度液
体溜めから外部へ連通する高密度液体出口流路とを備え
ている。
In order to achieve the above object, in the multistage centrifugal extractor according to the present invention, an introduction hole penetrating vertically is formed at the center of the bottom and an outlet hole penetrating circumferentially at a portion near the upper end. , A supply chamber surrounding the lower portion of the rotating drum in the circumferential direction, and a low density surrounding the upper portion of the rotating drum in the circumferential direction and the rotating portion closer to the opening. The liquid reservoir and the high-density liquid reservoir, and the high-density liquid provided at the upper end of the rotary drum and flowing into the rotary drum through the supply hole from the supply chamber into the rotary drum can be guided to the high-density liquid reservoir by centrifugal force accompanying rotation of the rotary drum. An outer weir and a low-density liquid that is provided near the upper end of the rotating drum so as to be located below the outer weir and that flows into the rotating drum from the supply chamber through the introduction hole by centrifugal force accompanying rotation of the rotating drum. Guide to low-density fluid reservoir through outlet hole A plurality of centrifugal extraction means each having an inner weir and a low-density liquid inlet flow path that is externally connected to the supply chamber of the centrifugal extraction means located at the forefront end, and between each centrifugal extraction means. And a low-density liquid transfer passage communicating from the low-density liquid reservoir of the centrifugal extraction means located on the front side to the supply chamber of the centrifugal extraction means located on the rear side; A low-density liquid outlet flow path communicating from the high-density liquid reservoir to the outside, a high-density liquid inlet flow path communicating from the outside to the supply chamber of the centrifugal extraction means located at the rearmost end, and located between and behind each centrifugal extraction means A high-density liquid transfer flow path communicating from the high-density liquid reservoir of the centrifugal extraction means located on the side to the supply chamber of the centrifugal extraction means located on the front side, and from the high-density liquid reservoir of the centrifugal extraction means located at the foremost end to the outside. High-density liquid communicating with And an outlet flow passage.

【0027】本発明の請求項2に記載の多段遠心抽出器
では、本発明の請求項1に記載の多段遠心抽出器の構成
に加えて、各回転胴を同一回転数で同方向へ回転させる
同調回転機構を備えている。
In the multistage centrifugal extractor according to the second aspect of the present invention, in addition to the configuration of the multistage centrifugal extractor according to the first aspect of the present invention, each rotating body is rotated in the same direction at the same rotational speed. A tuning rotation mechanism is provided.

【0028】本発明の請求項3に記載の多段遠心抽出器
では、本発明の請求項1あるいは請求項2に記載の多段
遠心抽出器の構成に加えて、供給室に連なり且つ回転胴
を周方向に取り囲み且つ回転胴寄り部分が開口した滞留
室を備えている。
In the multistage centrifugal extractor according to the third aspect of the present invention, in addition to the configuration of the multistage centrifugal extractor according to the first or second aspect of the present invention, the multistage centrifugal extractor is connected to the supply chamber and has a rotary drum. And a stagnation chamber which surrounds in the direction and is open at a portion close to the rotating body.

【0029】本発明の請求項1乃至請求項3に記載の多
段遠心抽出器のいずれにおいても、各遠心抽出手段のそ
れぞれの供給室で、低密度液体入口流路から各遠心抽出
手段及びその間の低密度液体移送流路を経て低密度液体
出口流路へ向う液体に含まれている物質が、高密度液体
入口流路から各遠心抽出手段及びその間の高密度液体移
送流路を経て高密度液体出口流路へ向う液体へ移行す
る。
In any one of the multistage centrifugal extractors according to the first to third aspects of the present invention, the supply chamber of each centrifugal extraction unit is connected to the low-density liquid inlet channel through each centrifugal extraction unit and between them. The substance contained in the liquid flowing to the low-density liquid outlet flow path through the low-density liquid transfer flow path passes through the centrifugal extraction means from the high-density liquid inlet flow path and the high-density liquid transfer path through the high-density liquid transfer flow path therebetween. Transfer to liquid going to outlet channel.

【0030】本発明の請求項2に記載の多段遠心抽出手
段においては、各遠心抽出手段の回転胴が、同調回転機
構により同一回転数で同一方向に回転する。
[0030] In the multistage centrifugal extraction means according to the second aspect of the present invention, the rotating drum of each centrifugal extraction means is rotated in the same direction at the same rotation speed by the synchronous rotation mechanism.

【0031】本発明の請求項3に記載の多段遠心抽出手
段においては、回転胴の回転に伴って供給室内の液体に
作用する遠心力を滞留室により緩和し、供給室内での液
位上昇を防止する。
[0031] In the multistage centrifugal extraction means according to the third aspect of the present invention, the centrifugal force acting on the liquid in the supply chamber with the rotation of the rotary drum is reduced by the retention chamber, and the liquid level rise in the supply chamber is reduced. To prevent.

【0032】[0032]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0033】図1から図6は本発明の多段遠心抽出器の
実施の形態の一例を示すものであり、図中、図7と同一
の符号を付した部分は同一物を表している。
FIGS. 1 to 6 show an embodiment of a multistage centrifugal extractor according to the present invention. In the drawing, the same reference numerals as those in FIG. 7 denote the same parts.

【0034】この多段遠心抽出器では、図7に示す遠心
抽出器と同様に、回転胴3、供給室4、液体溜め17,
18、外側堰11、内側堰12をそれぞれ備えた複数の
遠心抽出手段A,B,C,D,E,Fが、横方向に一列
に並ぶように、ケーシング本体25と蓋体26とにより
構成されるケーシング27に組み込まれている。
In this multi-stage centrifugal extractor, similarly to the centrifugal extractor shown in FIG. 7, the rotary drum 3, the supply chamber 4, the liquid reservoir 17,
18, a plurality of centrifugal extraction means A, B, C, D, E, and F each having an outer weir 11 and an inner weir 12 are constituted by a casing body 25 and a lid 26 so as to be arranged in a row in the horizontal direction. Is incorporated in the casing 27 to be manufactured.

【0035】ケーシング本体25には、溶融塩5が流通
する入口流路28、移送流路29及び出口流路30と、
溶融金属7が流通する入口流路31、移送流路32及び
出口流路33とが穿設されている。
The casing body 25 has an inlet passage 28, a transfer passage 29, and an outlet passage 30 through which the molten salt 5 flows.
An inlet channel 31, a transfer channel 32, and an outlet channel 33 through which the molten metal 7 flows are formed.

【0036】入口流路28は、ケーシング本体25の外
部と最前端に位置する遠心抽出手段Aの供給室4とを連
通している。
The inlet passage 28 communicates the outside of the casing body 25 with the supply chamber 4 of the centrifugal extraction means A located at the forefront end.

【0037】移送流路29は、遠心抽出手段A,B,
C,D,Eの液体溜め18とこれら遠心抽出手段A,
B,C,D,Eに隣接する他の遠心抽出手段B,C,
D,E,Fの供給室4とを連通している。
The transfer channel 29 includes centrifugal extraction means A, B,
C, D, E liquid reservoirs 18 and these centrifugal extraction means A,
Other centrifugal extraction means B, C, adjacent to B, C, D, E
The supply chambers 4 for D, E, and F are communicated.

【0038】出口流路30は、最後端に位置する遠心抽
出手段Fの液体溜め18とケーシング本体25の外部と
を連通している。
The outlet channel 30 communicates the liquid reservoir 18 of the centrifugal extraction means F located at the rearmost end with the outside of the casing body 25.

【0039】入口流路31は、ケーシング本体25の外
部と最後端に位置する遠心抽出手段Fの供給室4とを連
通している。
The inlet channel 31 communicates the outside of the casing body 25 with the supply chamber 4 of the centrifugal extraction means F located at the rearmost end.

【0040】移送流路32は、遠心抽出手段F,E,
D,C,Bの液体溜め17とこれら遠心抽出手段F,
E,D,C,Bに隣接する他の遠心抽出手段E,D,
C,B,Aの供給室4とを連通している。
The transfer channel 32 is provided with centrifugal extraction means F, E,
D, C, B liquid reservoirs 17 and these centrifugal extraction means F,
Other centrifugal extraction means E, D, adjacent to E, D, C, B
The C, B, and A supply chambers 4 are in communication.

【0041】出口流路33は、最前端に位置する遠心抽
出手段Aの液体溜め17とケーシング本体25の外部と
を連通している。
The outlet channel 33 communicates the liquid reservoir 17 of the centrifugal extraction means A located at the foremost end with the outside of the casing body 25.

【0042】ケーシング本体25内には、供給室4に連
なり且つ回転胴3を周方向に取り囲む内方が開口した滞
留室34が形成され、ケーシング本体25の底部には、
各供給室4に対応するプラグ35が取り付けられてい
る。
Inside the casing main body 25, there is formed a staying chamber 34 which is continuous with the supply chamber 4 and surrounds the rotary drum 3 in the circumferential direction.
A plug 35 corresponding to each supply chamber 4 is attached.

【0043】また、蓋体26には、入口流路28、移送
流路29及び出口流路30のそれぞれに対応するプラグ
36と、入口流路31、移送流路32及び出口流路33
に対応するプラグ37とが取り付けられている。
The lid 26 has plugs 36 corresponding to the inlet channel 28, the transfer channel 29 and the outlet channel 30, respectively, and the inlet channel 31, the transfer channel 32 and the outlet channel 33.
Are attached.

【0044】更に、ケーシング27の上方には、各遠心
抽出手段A,B,C,D,E,Fのそれぞれの駆動軸1
5に向って同軸に延びる複数の回転力伝達軸38を有す
る歯車方式の同調回転機構39が配置されている。
Further, above the casing 27, each drive shaft 1 of each of the centrifugal extraction means A, B, C, D, E and F is provided.
A gear type tuning rotation mechanism 39 having a plurality of rotation force transmission shafts 38 extending coaxially toward 5 is arranged.

【0045】同調回転機構39の入力軸40には、駆動
装置(図示せず)の出力軸41が連結されており、該出
力軸41が回転すると、各回転力伝達軸38が同一回転
数で同一方向へ回転するように構成されている。
An output shaft 41 of a driving device (not shown) is connected to an input shaft 40 of the tuning rotation mechanism 39. When the output shaft 41 rotates, each torque transmitting shaft 38 rotates at the same rotational speed. It is configured to rotate in the same direction.

【0046】この同調回転機構39は、支柱42を介し
てケーシング本体25に支持され、各回転力伝達軸38
は、それぞれの遠心抽出手段A,B,C,D,E,Fの
駆動軸15に連結されている。
The tuning rotation mechanism 39 is supported by the casing main body 25 via a support post 42,
Are connected to the drive shafts 15 of the respective centrifugal extraction means A, B, C, D, E and F.

【0047】図1から図6に示す多段遠心抽出器を用い
て溶融塩5から放射性物質を取り除く際には、駆動装置
を作動させて、該駆動装置の回転力を同調回転機構39
を介して各遠心抽出手段A,B,C,D,E,Fの駆動
軸15に伝達し、それぞれの回転胴3を同一回転数で同
一方向へ回転させる。
When removing radioactive substances from the molten salt 5 using the multi-stage centrifugal extractor shown in FIGS. 1 to 6, the driving device is operated and the rotational force of the driving device is adjusted by the tuning rotation mechanism 39.
To the drive shaft 15 of each of the centrifugal extraction means A, B, C, D, E, and F to rotate the respective rotating drums 3 in the same direction at the same rotation speed.

【0048】次いで、溶融塩5を入口流路28に供給す
ると、各遠心抽出手段A,B,C,D,E,F及びその
間の移送流路29を経て出口流路30へ向う溶融塩5の
流れが生じ、これと同時に、溶融金属7を入口流路31
に供給すると、各遠心抽出手段F,E,D,C,B,A
及びその間の移送流路32を経て出口流路33へ向う溶
融金属7の流れが生じる。
Next, when the molten salt 5 is supplied to the inlet channel 28, the molten salt 5 is directed to the outlet channel 30 via each of the centrifugal extraction means A, B, C, D, E, F and the transport channel 29 therebetween. At the same time, the molten metal 7 flows into the inlet channel 31.
, The centrifugal extraction means F, E, D, C, B, A
The flow of the molten metal 7 toward the outlet flow path 33 via the transfer flow path 32 therebetween is generated.

【0049】これにより、各遠心抽出手段A,B,C,
D,E,Fのそれぞれの供給室4に流入した溶融塩5及
び溶融金属7が、回転胴3の回転に伴って混合されなが
ら、供給室4の底部から導入孔1を経て回転胴3の内部
へ流入する。
Thus, each of the centrifugal extraction means A, B, C,
The molten salt 5 and the molten metal 7 that have flowed into the supply chambers 4 of D, E, and F are mixed with the rotation of the rotary drum 3 from the bottom of the supply chamber 4 through the introduction hole 1 while being mixed with the rotation of the rotary drum 3. It flows inside.

【0050】このとき、溶融塩5に含まれている放射性
物質が溶融金属7へ移行し、溶融塩5から放射性物質が
取り除かれる。
At this time, the radioactive substance contained in the molten salt 5 moves to the molten metal 7 and the radioactive substance is removed from the molten salt 5.

【0051】すなわち、遠心抽出手段A,B,C,D,
E,Fの順に流通する溶融塩5は、該溶融塩5とは逆方
向に遠心抽出手段F,E,D,C,B,Aの順に流通す
る溶融金属7によって、放射性物質が逐次取り除かれる
ことになる。
That is, the centrifugal extraction means A, B, C, D,
From the molten salt 5 flowing in the order of E and F, radioactive substances are sequentially removed by the molten metal 7 flowing in the order of the centrifugal extraction means F, E, D, C, B and A in the opposite direction to the molten salt 5. Will be.

【0052】また、各遠心抽出手段A,B,C,D,
E,Fにおいては、回転胴3を周方向に取り囲む滞留室
34により、回転胴3の回転に起因して供給室4内の溶
融塩5及び溶融金属7の混合液体に作用する遠心力が緩
和される。
Each of the centrifugal extraction means A, B, C, D,
In E and F, the centrifugal force acting on the liquid mixture of the molten salt 5 and the molten metal 7 in the supply chamber 4 due to the rotation of the rotary drum 3 is reduced by the retention chamber 34 surrounding the rotary drum 3 in the circumferential direction. Is done.

【0053】これにより、未分離の溶融塩5及び溶融金
属7の混合液体が、供給室4から液体溜め17へ漏洩す
ることが防止され、供給室4から回転胴3への混合流体
の流入が防止され、滞留室34内の混合液体に乱流が生
じて、溶融塩5から溶融金属7への放射性物質の移行が
促進される。
This prevents the unseparated liquid mixture of the molten salt 5 and the molten metal 7 from leaking from the supply chamber 4 to the liquid reservoir 17, and prevents the mixed fluid from flowing from the supply chamber 4 to the rotary drum 3. As a result, turbulence occurs in the mixed liquid in the retention chamber 34, and the transfer of the radioactive substance from the molten salt 5 to the molten metal 7 is promoted.

【0054】このように、図1から図6に示す多段遠心
抽出器では、各遠心抽出手段A,B,C,D,E,Fの
それぞれにおいて、入口流路28から各遠心抽出手段
A,B,C,D,E,F及びその間の移送流路29を経
て出口流路30へ向う溶融塩5に含まれている放射性物
質が、入口流路31から各遠心抽出手段F,E,D,
C,B,A及びその間の移送流路32を経て出口流路3
3へ向う溶融金属7へ移行するので、溶融塩5からの放
射性物質の除去を効率よく行える。
As described above, in the multistage centrifugal extractors shown in FIGS. 1 to 6, in each of the centrifugal extraction means A, B, C, D, E, and F, the centrifugal extraction means A, B, C, D, E, F, and radioactive substances contained in the molten salt 5 flowing to the outlet flow path 30 via the transfer flow path 29 therebetween are supplied from the inlet flow path 31 to the respective centrifugal extraction means F, E, D. ,
C, B, A and the outlet channel 3 via the transfer channel 32 between them
Since the transition to the molten metal 7 toward 3 occurs, the removal of radioactive substances from the molten salt 5 can be performed efficiently.

【0055】また、滞留室34により、各遠心抽出手段
A,B,C,D,E,Fのそれぞれの供給室4内におけ
る溶融塩及び溶融金属7の混合液体に作用する遠心力が
緩和されるので、回転胴3を高回転数で駆動して、溶融
塩5と溶融金属7の分離作業の効率向上を図ることが可
能になる。
The retention chamber 34 reduces the centrifugal force acting on the liquid mixture of the molten salt and the molten metal 7 in the supply chamber 4 of each of the centrifugal extraction means A, B, C, D, E and F. Therefore, it is possible to drive the rotating drum 3 at a high rotation speed to improve the efficiency of the separation work of the molten salt 5 and the molten metal 7.

【0056】更に、それぞれの回転胴3が、同調駆動機
構39により同一回転数で同一方向へ回転するので、各
遠心抽出手段A,B,C,D,E,Fにおける溶融塩5
と溶融金属7との分離効率が同等になり、液体送出量の
差に起因する漏洩が生じない。
Further, since each rotary drum 3 is rotated in the same direction at the same rotation speed by the tuning drive mechanism 39, the molten salt 5 in each of the centrifugal extraction means A, B, C, D, E, and F is rotated.
And the molten metal 7 have the same separation efficiency, and no leakage occurs due to the difference in the liquid delivery amount.

【0057】なお、本発明の多段遠心抽出器は上述した
実施の形態のみに限定されるものではなく、本発明の要
旨を逸脱しない範囲において変更を加え得ることは勿論
である。
The multi-stage centrifugal extractor of the present invention is not limited to the above-described embodiment, but may be modified without departing from the scope of the present invention.

【0058】[0058]

【発明の効果】以上述べたように、本発明の多段遠心抽
出器では下記のような種々の優れた効果を奏し得る。
As described above, the multistage centrifugal extractor of the present invention can provide various excellent effects as described below.

【0059】(1)本発明の請求項1乃至請求項3に記
載の多段遠心抽出器のいずれにおいても、各遠心抽出手
段のそれぞれの供給室で、低密度液体入口流路から各遠
心抽出手段及びその間の低密度液体移送流路を経て低密
度液体出口流路へ向う液体に含まれている物質が、高密
度液体入口流路から各遠心抽出手段及びその間の高密度
液体移送流路を経て高密度液体出口流路へ向う液体へ移
行するので、一方の液体から他方の液体への物質の移行
を効率よく行うことができる。
(1) In any one of the multistage centrifugal extractors according to the first to third aspects of the present invention, each supply chamber of each centrifugal extraction unit is connected to each centrifugal extraction unit from the low-density liquid inlet channel. And the substance contained in the liquid flowing to the low-density liquid outlet flow path via the low-density liquid transfer flow path therebetween, from the high-density liquid inlet flow path through each centrifugal extraction means and the high-density liquid transfer flow path therebetween Since the liquid is transferred to the high-density liquid outlet flow path, the transfer of the substance from one liquid to the other liquid can be performed efficiently.

【0060】(2)本発明の請求項2に記載の多段遠心
抽出器においては、それぞれの回転胴が、同調回転機構
により同一回転数で同一方向に回転するので、各遠心抽
出手段における2種類の液体の分離効率が同等になり、
液体送出量の差に起因する漏洩が生じない。
(2) In the multistage centrifugal extractor according to the second aspect of the present invention, since each rotating body is rotated in the same direction at the same rotation speed by the synchronous rotation mechanism, two types of centrifugal extraction means are used. Liquid separation efficiency becomes equal,
No leakage due to the difference in liquid delivery rate occurs.

【0061】(3)本発明の請求項3に記載の多段遠心
抽出器においては、回転胴の回転に伴って供給室内の液
体に作用する遠心力を滞留室により緩和し、供給室内で
の液位上昇を防止するので、回転胴を高回転させること
ができ、2種類の液体の分離効率の向上を図ることがで
きる。
(3) In the multistage centrifugal extractor according to claim 3 of the present invention, the centrifugal force acting on the liquid in the supply chamber with the rotation of the rotary drum is alleviated by the retention chamber, and the liquid in the supply chamber is reduced. Since the rise in the position is prevented, the rotating drum can be rotated at a high speed, and the separation efficiency of the two types of liquids can be improved.

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

【図1】本発明の多段遠心抽出器の実施の形態の一例を
示す水平断面図である。
FIG. 1 is a horizontal sectional view showing an example of an embodiment of a multistage centrifugal extractor of the present invention.

【図2】図1のII−II矢視図である。FIG. 2 is a view taken in the direction of arrows II-II in FIG.

【図3】図1のIII−III矢視図である。FIG. 3 is a view taken in the direction of arrows III-III in FIG. 1;

【図4】図1のIV−IV矢視図である。FIG. 4 is a view taken in the direction of arrows IV-IV in FIG. 1;

【図5】図1のV−V矢視図である。FIG. 5 is a view taken in the direction of arrows VV in FIG. 1;

【図6】図1のVI−VI矢視図である。FIG. 6 is a view taken in the direction of arrows VI-VI in FIG. 1;

【図7】近年提案されている遠心抽出器の一例を示す縦
断面図である。
FIG. 7 is a longitudinal sectional view showing an example of a centrifugal extractor proposed in recent years.

【符号の説明】[Explanation of symbols]

1 導入孔 2 流出孔 3 回転胴 4 供給室 11 外側堰 12 内側堰 17 液体溜め(低密度液体溜め) 18 液体溜め(高密度液体溜め) 28 入口流路(低密度液体入口流路) 29 移送流路(低密度液体移送流路) 30 出口流路(低密度液体出口流路) 31 入口流路(高密度液体入口流路) 32 移送流路(高密度液体移送流路) 33 出口流路(高密度液体出口流路) 34 滞留室 39 同調回転機構 A,B,C,D,E,F 遠心抽出手段 DESCRIPTION OF SYMBOLS 1 Introducing hole 2 Outflow hole 3 Rotating drum 4 Supply chamber 11 Outer weir 12 Inner weir 17 Liquid reservoir (low-density liquid reservoir) 18 Liquid reservoir (high-density liquid reservoir) 28 Inlet flow path (low-density liquid inlet flow path) 29 Transfer Flow path (low-density liquid transfer flow path) 30 Outlet flow path (low-density liquid outlet flow path) 31 Inlet flow path (high-density liquid inlet flow path) 32 Transfer flow path (high-density liquid transfer flow path) 33 Outlet flow path (High-density liquid outlet channel) 34 Retention chamber 39 Synchronous rotation mechanism A, B, C, D, E, F Centrifugal extraction means

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 底部中央に上下方向へ貫通する導入孔が
穿設され且つ上端寄り部分に周方向へ貫通する流出孔が
穿設された略円筒状の回転胴と、回転胴の下側寄り部分
を周方向に取り囲む供給室と、回転胴の上側寄り部分を
周方向に取り囲み且つ回転胴寄り部分が開口した低密度
液体溜め及び高密度液体溜めと、回転胴の上端に設けら
れ且つ供給室から導入孔を経て回転胴内に流入する高密
度液体を回転胴の回転に伴う遠心力により高密度液体溜
めへ導き得る外側堰と、該外側堰の下方に位置するよう
に回転胴の上端近傍部分に設けられ且つ供給室から導入
孔を経て回転胴内に流入する低密度液体を回転胴の回転
に伴う遠心力により流出孔を介して低密度流体溜めへ導
き得る内側堰とをそれぞれ有する複数の遠心抽出手段が
横方向に一列に配置され、最前端に位置する遠心抽出手
段の供給室へ外部から連通する低密度液体入口流路と、
各遠心抽出手段間に位置し且つ前方側に位置する遠心抽
出手段の低密度液体溜めから後方側に位置する遠心抽出
手段の供給室へ連通する低密度液体移送流路と、最後端
に位置する遠心抽出手段の低密度液体溜めから外部へ連
通する低密度液体出口流路と、最後端に位置する遠心抽
出手段の供給室へ外部から連通する高密度液体入口流路
と、各遠心抽出手段間に位置し且つ後方側に位置する遠
心抽出手段の高密度液体溜めから前方側に位置する遠心
抽出手段の供給室へ連通する高密度液体移送流路と、最
前端に位置する遠心抽出手段の高密度液体溜めから外部
へ連通する高密度液体出口流路とを備えてなることを特
徴とする多段遠心抽出器。
1. A substantially cylindrical rotating drum having a bottom hole formed with an introduction hole penetrating in the vertical direction and an outlet hole penetrating in the circumferential direction at a portion near the upper end, and a lower portion near the rotating drum. A supply chamber surrounding the portion in the circumferential direction, a low-density liquid reservoir and a high-density liquid reservoir surrounding the upper portion of the rotary drum in the circumferential direction and opening the portion closer to the rotary drum, and a supply chamber provided at the upper end of the rotary drum. An outer weir that can guide the high-density liquid flowing into the rotary drum through the introduction hole to the high-density liquid reservoir by centrifugal force accompanying rotation of the rotary drum, and near the upper end of the rotary drum to be located below the outer weir And a plurality of inner weirs provided in the portion and capable of guiding the low-density liquid flowing into the rotary drum from the supply chamber through the inlet hole to the low-density fluid reservoir through the outlet hole by centrifugal force accompanying rotation of the rotary drum. Centrifugal extraction means are arranged in a row in the horizontal direction And a low-density liquid inlet flow path that is externally connected to the supply chamber of the centrifugal extraction means located at the forefront end,
A low-density liquid transfer passage communicating between the low-density liquid reservoir of the centrifugal extraction means located on the front side and located between the centrifugal extraction means and the supply chamber of the centrifugal extraction means located on the rear side; A low-density liquid outlet flow path communicating from the low-density liquid reservoir of the centrifugal extraction means to the outside; a high-density liquid inlet flow path communicating from the outside to the supply chamber of the centrifugal extraction means located at the rearmost end; And a high-density liquid transfer passage communicating from the high-density liquid reservoir of the centrifugal extraction means located on the rear side to the supply chamber of the centrifugal extraction means located on the front side; A multi-stage centrifugal extractor comprising: a high-density liquid outlet flow path communicating from the high-density liquid reservoir to the outside.
【請求項2】 各回転胴を同一回転数で同方向へ回転さ
せる同調回転機構を備えた請求項1に記載の多段遠心抽
出器。
2. The multi-stage centrifugal extractor according to claim 1, further comprising a tuning rotation mechanism for rotating each rotating drum in the same direction at the same rotation speed.
【請求項3】 供給室に連なり且つ回転胴を周方向に取
り囲み且つ回転胴寄り部分が開口した滞留室を備えた請
求項1あるいは請求項2のいずれかに記載の多段遠心抽
出器。
3. The multi-stage centrifugal extractor according to claim 1, further comprising a staying chamber connected to the supply chamber, surrounding the rotating drum in the circumferential direction, and having an opening at a portion close to the rotating drum.
JP9614798A 1998-04-08 1998-04-08 Multi-stage centrifugal extractor Pending JPH11290606A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9614798A JPH11290606A (en) 1998-04-08 1998-04-08 Multi-stage centrifugal extractor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9614798A JPH11290606A (en) 1998-04-08 1998-04-08 Multi-stage centrifugal extractor

Publications (1)

Publication Number Publication Date
JPH11290606A true JPH11290606A (en) 1999-10-26

Family

ID=14157278

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9614798A Pending JPH11290606A (en) 1998-04-08 1998-04-08 Multi-stage centrifugal extractor

Country Status (1)

Country Link
JP (1) JPH11290606A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012000582A (en) * 2010-06-18 2012-01-05 Nano Science:Kk Method for producing water for living body containing stabilized nanobubbles of gas and water for living body
CN104874201A (en) * 2014-02-27 2015-09-02 浦华环保有限公司 Combined centrifugal extractor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012000582A (en) * 2010-06-18 2012-01-05 Nano Science:Kk Method for producing water for living body containing stabilized nanobubbles of gas and water for living body
CN104874201A (en) * 2014-02-27 2015-09-02 浦华环保有限公司 Combined centrifugal extractor

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