JPH08105997A - Liquid metal purification device - Google Patents

Liquid metal purification device

Info

Publication number
JPH08105997A
JPH08105997A JP6241335A JP24133594A JPH08105997A JP H08105997 A JPH08105997 A JP H08105997A JP 6241335 A JP6241335 A JP 6241335A JP 24133594 A JP24133594 A JP 24133594A JP H08105997 A JPH08105997 A JP H08105997A
Authority
JP
Japan
Prior art keywords
liquid metal
hot gas
pipe
liquid
tank
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
JP6241335A
Other languages
Japanese (ja)
Inventor
Akira Nishikawa
明 西川
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 JP6241335A priority Critical patent/JPH08105997A/en
Publication of JPH08105997A publication Critical patent/JPH08105997A/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

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE: To eliminate the clogging of an impurity arresting device and restore the function thereof. CONSTITUTION: When an impurity arresting device 11 is clogged with deposited impurities as a result of a long-term operation, valves 27 and 28 fitted to a liquid-metal feed pipe 13 and a liquid-metal discharge pipe 14 are closed to stop the feed and discharge of liquid-metal. Then, heated gas is supplied from a hot gas feed port 19, and circulated to the pipe 14, a liquid-metal tank 6, the device 11, a cooling device 33 and the pipe 13 in order. The gas is finally, discharged from a hot gas discharge port 20. According to this construction, impurities deposited in the device 11 are melted and collected into a liquid discharge tank 26.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、高速増殖炉や核融合炉
などの施設で冷却材などとして使われるリチウムやナト
リウムなどの液体金属から不純物を除去するための液体
金属純化装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquid metal purifying apparatus for removing impurities from liquid metals such as lithium and sodium used as coolants in facilities such as fast breeder reactors and fusion reactors. .

【0002】[0002]

【従来の技術】図3は、従来の液体金属純化装置を示す
ものである。
2. Description of the Related Art FIG. 3 shows a conventional liquid metal purifying apparatus.

【0003】ほぼ円筒容器状をした液体金属純化装置本
体1の内部に上下に間隔を置いて一対の仕切板2,3を
設け、上部の仕切板2の上部と下部の仕切板3の下部に
それぞれ冷媒ガス出口ヘッダ4と冷媒ガス入口ヘッダ5
を形成すると共に、上下の仕切板2,3間に液体金属槽
6を形成する。
A pair of partition plates 2 and 3 are provided inside the liquid metal purifying apparatus main body 1 in the shape of a substantially cylindrical container with a space between the upper and lower parts. The upper partition plate 2 and the lower partition plate 3 are provided below the partition plates 2 and 3, respectively. Refrigerant gas outlet header 4 and refrigerant gas inlet header 5 respectively
And the liquid metal tank 6 is formed between the upper and lower partition plates 2 and 3.

【0004】該液体金属槽6内における外壁に近い位置
に、上下方向へ延びる伝熱管7を互いに間隔を置いて周
方向に複数本配列すると共に、各伝熱管7の両端を、対
応する仕切板2,3に貫通させて、それぞれ冷媒ガス入
口ヘッダ5及び冷媒ガス出口ヘッダ4と連通させて、降
温装置33を構成する。
A plurality of heat transfer tubes 7 extending in the vertical direction are arranged at intervals in the circumferential direction at positions near the outer wall in the liquid metal tank 6, and both ends of each heat transfer tube 7 are provided with corresponding partition plates. The cooling device 33 is configured by penetrating the second and third passages and communicating with the refrigerant gas inlet header 5 and the refrigerant gas outlet header 4, respectively.

【0005】又、液体金属槽6の内部に、上部の仕切板
2に対し間隙8を有して支持板9を配置し、該支持板9
の外縁部に、各伝熱管7の内側に位置し、且つ、下方へ
延びる円筒形の断熱材10を取付ける。
Further, a support plate 9 is arranged inside the liquid metal tank 6 with a gap 8 between the upper partition plate 2 and the support plate 9.
The cylindrical heat insulating material 10 which is located inside each heat transfer tube 7 and extends downward is attached to the outer edge portion of the.

【0006】更に、支持板9の下面に、断熱材10の内
側に位置する、円筒状の捕集用金網11などの不純物捕
集装置を取付け、捕集用金網11の下端を閉止板12或
いは金網で閉止する。
Further, an impurity collecting device such as a cylindrical collecting wire net 11 located inside the heat insulating material 10 is attached to the lower surface of the support plate 9, and the lower end of the collecting wire net 11 is closed by a closing plate 12 or Close with wire mesh.

【0007】更に又、冷媒ガス出口ヘッダ4及び上部の
仕切板2を貫通して、外部と液体金属槽6の支持板9上
方の間隙8との間を連通する液体金属供給管13を設け
ると共に、液体金属供給管13及び支持板9を貫通し
て、外部と捕集用金網11の内部との間を連通する液体
金属排出管14を設ける。
Further, a liquid metal supply pipe 13 is provided which penetrates the refrigerant gas outlet header 4 and the upper partition plate 2 and communicates between the outside and the gap 8 above the support plate 9 of the liquid metal tank 6. A liquid metal discharge pipe 14 that penetrates the liquid metal supply pipe 13 and the support plate 9 and connects the outside and the inside of the collection wire net 11 is provided.

【0008】尚、15はアルゴンなどの不活性ガスなど
による冷媒ガス、16は冷媒ガス15を冷媒ガス入口ヘ
ッダ5へ供給する冷媒ガス供給管、17は冷媒ガス15
を冷媒ガス出口ヘッダ4から排出する冷媒ガス排出管、
18はリチウムやナトリウムやカリウムやガリウムなど
の液体金属である。
Reference numeral 15 is a refrigerant gas such as an inert gas such as argon, 16 is a refrigerant gas supply pipe for supplying the refrigerant gas 15 to the refrigerant gas inlet header 5, and 17 is a refrigerant gas 15
For discharging the refrigerant from the refrigerant gas outlet header 4,
18 is a liquid metal such as lithium, sodium, potassium or gallium.

【0009】又、液体金属排出管14には、捕集用金網
11内の部分に図示しない貫通孔が多数穿設されてい
る。
Further, the liquid metal discharge pipe 14 is provided with a large number of through holes (not shown) in a portion inside the collecting wire net 11.

【0010】上記液体金属純化装置は、高速増殖炉や核
融合炉などの施設における、液体金属18を流通させる
流路の途中に取付けられる。
The above-mentioned liquid metal purifying apparatus is attached in the middle of a flow path for circulating the liquid metal 18 in a facility such as a fast breeder reactor or a nuclear fusion reactor.

【0011】そして、リチウムやナトリウムやカリウム
やガリウムなどの液体金属18から不純物を除去する場
合、先ず、液体金属18が液体金属供給管13へ導かれ
る。
When removing impurities from the liquid metal 18 such as lithium, sodium, potassium or gallium, first, the liquid metal 18 is introduced into the liquid metal supply pipe 13.

【0012】すると、液体金属18は、液体金属供給管
13から液体金属槽6における上部の仕切板2と支持板
9との間隙8へ供給され、間隙8から外壁と断熱材10
との間へと送られる。
Then, the liquid metal 18 is supplied from the liquid metal supply pipe 13 to the gap 8 between the upper partition plate 2 and the support plate 9 in the liquid metal tank 6, and the gap 8 provides the outer wall and the heat insulating material 10.
Sent to and from.

【0013】この時、アルゴンなどの不活性ガスからな
る冷媒ガス15を、冷媒ガス供給管16から冷媒ガス入
口ヘッダ5へ供給すると、冷媒ガス15は冷媒ガス入口
ヘッダ5から伝熱管7へ通され、外壁と断熱材10との
間を流れる液体金属18の温度を摂氏400度から20
0度程度にまで低下させ、液体金属18の溶解度を低下
させる。
At this time, when the refrigerant gas 15 made of an inert gas such as argon is supplied from the refrigerant gas supply pipe 16 to the refrigerant gas inlet header 5, the refrigerant gas 15 is passed from the refrigerant gas inlet header 5 to the heat transfer pipe 7. , The temperature of the liquid metal 18 flowing between the outer wall and the heat insulating material 10 from 400 degrees Celsius to 20 degrees Celsius.
The solubility of the liquid metal 18 is reduced to about 0 degree.

【0014】その後、冷媒ガス15は、各伝熱管7から
冷媒ガス出口ヘッダ4へ取出されて、冷媒ガス出口ヘッ
ダ4から冷媒ガス排出管17へ排出される。
After that, the refrigerant gas 15 is taken out from each heat transfer pipe 7 to the refrigerant gas outlet header 4, and is discharged from the refrigerant gas outlet header 4 to the refrigerant gas discharge pipe 17.

【0015】一方、冷媒ガス15により溶解度が低下さ
れた液体金属18は、断熱材10の下端をくぐって、断
熱材10の内側へと導かれ、断熱材10の内側に設けら
れた捕集用金網11を通過した後、液体金属排出管14
から外部へ送り出される。
On the other hand, the liquid metal 18 whose solubility has been reduced by the refrigerant gas 15 is guided to the inside of the heat insulating material 10 through the lower end of the heat insulating material 10, and is collected inside the heat insulating material 10. After passing through the metal net 11, the liquid metal discharge pipe 14
Sent to the outside.

【0016】そして、液体金属18は溶解度が低下され
ているため、捕集用金網11を通過する際に、液体金属
18中に溶存されている酸素などの不純物が、捕集用金
網11に付着され、不純物を核として液体金属18の酸
化物の結晶などが生成されることにより不純物が捕集除
去される。
Since the liquid metal 18 has a reduced solubility, impurities such as oxygen dissolved in the liquid metal 18 adhere to the collecting wire net 11 when passing through the collecting wire net 11. The impurities are collected and removed by producing crystals of the oxide of the liquid metal 18 with the impurities as nuclei.

【0017】[0017]

【発明が解決しようとする課題】しかしながら、上記従
来の液体金属純化装置には、以下のような問題があっ
た。
However, the above-mentioned conventional liquid metal purifying apparatus has the following problems.

【0018】即ち、液体金属18の温度を下げて、溶存
酸素を捕集用金網11に析出させるようにしていたが、
長期間の運転により、酸化物の結晶が成長して捕集用金
網11の目を詰まらせてしまい、圧力損失が高くなって
性能の低下を招いたり、目詰まりによって捕集用金網1
1の閉塞を生じさせたりする。
That is, the temperature of the liquid metal 18 is lowered so that the dissolved oxygen is deposited on the collecting wire net 11.
Owing to long-term operation, oxide crystals grow and clog the catching wire netting 11, resulting in high pressure loss and deterioration of performance.
It causes 1 blockage.

【0019】本発明は、上述の実情に鑑み、捕集用金網
の目詰まりを除去し、機能を回復し得るようにした液体
金属純化装置を提供することを目的とするものである。
In view of the above situation, it is an object of the present invention to provide a liquid metal purifying apparatus capable of removing the clogging of a collecting wire net and recovering its function.

【0020】[0020]

【課題を解決するための手段】本発明は、液体金属供給
管と液体金属排出管を接続された液体金属槽の内部に降
温装置と不純物捕集装置を配置された液体金属純化装置
において、液体金属供給管と液体金属排出管に液体金属
の給排を停止させる弁を設けると共に、液体金属供給管
と液体金属排出管に、液体金属槽内部に対して加熱され
たガスを液体金属とは逆方向に流すホットガス排出口と
ホットガス供給口をそれぞれ形成し、更に、液体金属槽
に排液タンクを接続したことを特徴とする液体金属純化
装置にかかるものである。
The present invention relates to a liquid metal purifying apparatus in which a temperature lowering device and an impurity collecting device are arranged inside a liquid metal tank to which a liquid metal supply pipe and a liquid metal discharge pipe are connected. The metal supply pipe and the liquid metal discharge pipe are provided with valves for stopping the supply and discharge of the liquid metal, and the liquid metal supply pipe and the liquid metal discharge pipe are arranged so that the gas heated inside the liquid metal tank is opposite to the liquid metal. The present invention relates to a liquid metal purifying apparatus, characterized in that a hot gas discharge port and a hot gas supply port that flow in a direction are respectively formed, and a drainage tank is connected to a liquid metal tank.

【0021】この場合において、ホットガス排出口とホ
ットガス供給口の間をホットガス流路で接続し、ホット
ガス流路の途中にガス供給源と循環装置と加熱装置を設
けるようにしても良い。
In this case, the hot gas discharge port and the hot gas supply port may be connected by a hot gas passage, and a gas supply source, a circulation device and a heating device may be provided in the middle of the hot gas passage. .

【0022】[0022]

【作用】本発明の作用は以下の通りである。The operation of the present invention is as follows.

【0023】先ず、液体金属は、液体金属供給管から液
体金属槽内へ入り、液体金属槽内を降温装置、不純物捕
集装置の順に通過して、液体金属排出管から排出され
る。
First, the liquid metal enters the liquid metal tank from the liquid metal supply pipe, passes through the liquid metal tank through the temperature lowering device and the impurity collecting device in this order, and is discharged from the liquid metal discharge pipe.

【0024】この際、液体金属は、降温装置で温度を低
下され、溶解度を低下されているので、不純物は不純物
捕集装置に析出して容易に除去される。
At this time, since the temperature of the liquid metal is lowered by the temperature lowering device and the solubility thereof is lowered, the impurities are deposited in the impurity trapping device and easily removed.

【0025】長期間の運転により、析出した不純物で不
純物捕集装置に目詰まりが生じたら、液体金属供給管及
び液体金属排出管に設けられた弁を閉じて液体金属の給
排を停止させ、ホットガス供給口から加熱されたガスを
供給して、液体金属排出管、液体金属槽、不純物捕集装
置、降温装置、液体金属供給管の順に流し、ホットガス
排出口から排出させることにより、不純物捕集装置に析
出した不純物を溶かして、排液タンクに集める。
When the impurity collector is clogged with the deposited impurities due to long-term operation, the valves provided in the liquid metal supply pipe and the liquid metal discharge pipe are closed to stop the supply and discharge of the liquid metal, The heated gas is supplied from the hot gas supply port, and the liquid metal discharge pipe, the liquid metal tank, the impurity collecting device, the temperature lowering device, and the liquid metal supply pipe are flowed in this order to discharge the hot gas from the hot gas discharge port. The impurities deposited in the collector are melted and collected in the drainage tank.

【0026】これにより、不純物捕集装置の目詰まりが
解消され、不純物除去機能が回復される。
As a result, the clogging of the impurity collector is eliminated, and the impurity removing function is restored.

【0027】又、ホットガス排出口とホットガス供給口
の間をホットガス流路で接続し、ホットガス流路の途中
にガス供給源と循環装置と加熱装置を設けることによ
り、ガスを少ない量で循環使用することができる。
Further, the hot gas discharge port and the hot gas supply port are connected by a hot gas flow passage, and a gas supply source, a circulation device and a heating device are provided in the middle of the hot gas flow passage to reduce the amount of gas. It can be used in circulation.

【0028】[0028]

【実施例】以下、本発明の実施例を図面を参照しつつ説
明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0029】図1・図2は、本発明の一実施例である。1 and 2 show an embodiment of the present invention.

【0030】ほぼ円筒容器状をした液体金属純化装置本
体1の内部に上下に間隔を置いて一対の仕切板2,3を
設け、上部の仕切板2の上部と下部の仕切板3の下部に
それぞれ冷媒ガス出口ヘッダ4と冷媒ガス入口ヘッダ5
を形成すると共に、上下の仕切板2,3間に液体金属槽
6を形成する。
A pair of partition plates 2 and 3 are provided inside the main body 1 of the liquid metal purifying apparatus in the shape of a substantially cylindrical container and are vertically spaced from each other. Refrigerant gas outlet header 4 and refrigerant gas inlet header 5 respectively
And the liquid metal tank 6 is formed between the upper and lower partition plates 2 and 3.

【0031】該液体金属槽6内における外壁に近い位置
に、上下方向へ延びる伝熱管7を互いに間隔を置いて周
方向に複数本配列すると共に、各伝熱管7の両端を、対
応する仕切板2,3に貫通させて、それぞれ冷媒ガス入
口ヘッダ5及び冷媒ガス出口ヘッダ4と連通させ、降温
装置33を構成する。
A plurality of heat transfer tubes 7 extending in the vertical direction are arranged at intervals in the circumferential direction at positions near the outer wall in the liquid metal tank 6, and both ends of each heat transfer tube 7 are provided with corresponding partition plates. The cooling gas inlet header 5 and the refrigerant gas outlet header 4 are communicated with each other by penetrating the second and third portions to form the temperature lowering device 33.

【0032】又、液体金属槽6の内部に、上部の仕切板
2に対し間隙8を有して支持板9を配置し、該支持板9
の外縁部に、各伝熱管7の内側に位置し、且つ、下方へ
延びる円筒形の断熱材10を取付ける。
A support plate 9 is disposed inside the liquid metal tank 6 with a gap 8 between the upper partition plate 2 and the support plate 9.
The cylindrical heat insulating material 10 which is located inside each heat transfer tube 7 and extends downward is attached to the outer edge portion of the.

【0033】更に、支持板9の下面に、断熱材10の内
側に位置する、円筒状の捕集用金網11などの不純物捕
集装置を取付け、捕集用金網11の下端を閉止板12或
いは金網で閉止する。
Further, an impurity trapping device such as a cylindrical trapping net 11 located inside the heat insulating material 10 is attached to the lower surface of the support plate 9, and the lower end of the trapping net 11 is closed by a closing plate 12 or. Close with wire mesh.

【0034】更に又、冷媒ガス出口ヘッダ4及び上部の
仕切板2を貫通して、外部と液体金属槽6の支持板9上
方の間隙8との間を連通する液体金属供給管13を設け
ると共に、液体金属供給管13及び支持板9を貫通し
て、外部と捕集用金網11の内部との間を連通する液体
金属排出管14を設ける。
Further, a liquid metal supply pipe 13 is provided which penetrates the refrigerant gas outlet header 4 and the upper partition plate 2 and communicates between the outside and the gap 8 above the support plate 9 of the liquid metal tank 6. A liquid metal discharge pipe 14 that penetrates the liquid metal supply pipe 13 and the support plate 9 and connects the outside and the inside of the collection wire net 11 is provided.

【0035】尚、15はアルゴンなどの不活性ガスなど
による冷媒ガス、16は冷媒ガス15を冷媒ガス入口ヘ
ッダ5へ供給する冷媒ガス供給管、17は冷媒ガス15
を冷媒ガス出口ヘッダ4から排出する冷媒ガス排出管、
18はリチウムやナトリウムやカリウムやガリウムなど
の液体金属である。
Reference numeral 15 is a refrigerant gas such as an inert gas such as argon, 16 is a refrigerant gas supply pipe for supplying the refrigerant gas 15 to the refrigerant gas inlet header 5, and 17 is a refrigerant gas 15
For discharging the refrigerant from the refrigerant gas outlet header 4,
18 is a liquid metal such as lithium, sodium, potassium or gallium.

【0036】又、液体金属排出管14には、捕集用金網
11内の部分に図示しない貫通孔が多数穿設されてい
る。
The liquid metal discharge pipe 14 is provided with a large number of through holes (not shown) in a portion inside the collection wire net 11.

【0037】本発明では、上記に加えて、液体金属排出
管14にホットガス供給口19を設け、液体金属供給管
13にホットガス排出口20を設けて、ホットガス供給
口19とホットガス排出口20の間にホットガス流路2
1を接続し、ホットガス流路21の途中に、アルゴンな
どの不活性ガスを貯留するガスボンベなどのガス供給源
22と、不活性ガスを循環させるブロワなどの循環装置
23と、ヒータ等の加熱装置24を設ける。
In the present invention, in addition to the above, the hot gas supply port 19 is provided in the liquid metal discharge pipe 14, the hot gas discharge port 20 is provided in the liquid metal supply pipe 13, and the hot gas supply port 19 and the hot gas discharge port 19 are provided. Hot gas flow path 2 between the outlets 20
1, a gas supply source 22 such as a gas cylinder that stores an inert gas such as argon, a circulation device 23 such as a blower that circulates the inert gas, and a heating device such as a heater in the middle of the hot gas passage 21. A device 24 is provided.

【0038】尚、27は液体金属供給管13の途中に設
けられた弁、28は液体金属排出管14の途中に設けら
れた弁、29,30はホットガス流路21の入出側にそ
れぞれ設けられた弁、31は排液管25の途中に設けら
れた弁、32はガス供給源22に取付けられた弁であ
る。
Incidentally, 27 is a valve provided in the middle of the liquid metal supply pipe 13, 28 is a valve provided in the middle of the liquid metal discharge pipe 14, and 29 and 30 are respectively provided at the inlet and outlet sides of the hot gas passage 21. The valve 31 is a valve provided in the middle of the drain pipe 25, and the valve 32 is attached to the gas supply source 22.

【0039】そして、上記液体金属純化装置は、高速増
殖炉や核融合炉などの施設における、液体金属18を流
通させる流路の途中に取付けられる。
The liquid metal purifying device is attached in the middle of a flow path for circulating the liquid metal 18 in a facility such as a fast breeder reactor or a fusion reactor.

【0040】次に、作動について説明する。Next, the operation will be described.

【0041】リチウムやナトリウムやカリウムやガリウ
ムなどの液体金属18から不純物を除去する場合、図1
に示すように、先ず、弁27,28を開け、弁29〜3
2を閉じておく。
In the case of removing impurities from the liquid metal 18 such as lithium, sodium, potassium and gallium, as shown in FIG.
First, the valves 27 and 28 are opened to open the valves 29 to 3 as shown in FIG.
Keep 2 closed.

【0042】すると、高速増殖炉や核融合炉などの施設
における、液体金属18を流通させるための流路を流れ
ている液体金属18は、先ず、液体金属供給管13へ導
かれ、液体金属供給管13から液体金属槽6における上
部の仕切板2と支持板9との間隙8へ供給され、間隙8
から外壁と断熱材10との間へと送られる。
Then, the liquid metal 18 flowing through the flow path for flowing the liquid metal 18 in a facility such as a fast breeder reactor or a nuclear fusion reactor is first guided to the liquid metal supply pipe 13 to supply the liquid metal. It is supplied from the pipe 13 to the gap 8 between the upper partition plate 2 and the support plate 9 in the liquid metal tank 6, and the gap 8
From the outer wall to the heat insulating material 10.

【0043】この時、アルゴンなどの不活性ガスからな
る冷媒ガス15を、冷媒ガス供給管16から冷媒ガス入
口ヘッダ5へ供給すると、冷媒ガス15は冷媒ガス入口
ヘッダ5から伝熱管7へ通され、外壁と断熱材10との
間を流れる液体金属18の温度を摂氏400度から20
0度程度にまで低下させ、液体金属18の溶解度を低下
させる。
At this time, when the refrigerant gas 15 made of an inert gas such as argon is supplied from the refrigerant gas supply pipe 16 to the refrigerant gas inlet header 5, the refrigerant gas 15 is passed from the refrigerant gas inlet header 5 to the heat transfer pipe 7. , The temperature of the liquid metal 18 flowing between the outer wall and the heat insulating material 10 from 400 degrees Celsius to 20 degrees Celsius.
The solubility of the liquid metal 18 is reduced to about 0 degree.

【0044】その後、冷媒ガス15は、各伝熱管7から
冷媒ガス出口ヘッダ4へ取出されて、冷媒ガス出口ヘッ
ダ4から冷媒ガス排出管17へ排出される。
After that, the refrigerant gas 15 is taken out from each heat transfer pipe 7 to the refrigerant gas outlet header 4, and is discharged from the refrigerant gas outlet header 4 to the refrigerant gas discharge pipe 17.

【0045】一方、冷媒ガス15により溶解度が低下さ
れた液体金属18は、断熱材10の下端をくぐって、断
熱材10の内側へと導かれ、断熱材10の内側に設けら
れた捕集用金網11を通過した後、液体金属排出管14
から高速増殖炉や核融合炉などの施設における、液体金
属18を流通させる流路へ送り出される。
On the other hand, the liquid metal 18 whose solubility has been reduced by the refrigerant gas 15 is guided to the inside of the heat insulating material 10 through the lower end of the heat insulating material 10, and is collected inside the heat insulating material 10. After passing through the metal net 11, the liquid metal discharge pipe 14
Is sent to a flow path for circulating the liquid metal 18 in a facility such as a fast breeder reactor or a fusion reactor.

【0046】そして、液体金属18は溶解度が低下され
ているため、捕集用金網11を通過する際に、液体金属
18中に溶存されている酸素などの不純物が、捕集用金
網11に付着され、不純物を核として液体金属18の酸
化物の結晶などが生成されることにより不純物が捕集除
去される。
Since the liquid metal 18 has a reduced solubility, impurities such as oxygen dissolved in the liquid metal 18 adhere to the collecting wire net 11 when passing through the collecting wire net 11. The impurities are collected and removed by producing crystals of the oxide of the liquid metal 18 with the impurities as nuclei.

【0047】長期間の運転により、酸化物の結晶が成長
して捕集用金網11の目が詰まったら、弁27,28を
閉じて液体金属18の給排を停止し、冷媒ガス15の給
排を停止する。
When oxide crystals grow due to long-term operation and the trapping wire netting 11 is clogged, the valves 27 and 28 are closed to stop the supply and discharge of the liquid metal 18 and supply the refrigerant gas 15. Stop draining.

【0048】次に、弁29〜32を開けて、ブロワなど
の循環装置23を駆動し、ガスボンベなどのガス供給源
22からアルゴンなどの不活性ガスをホットガス流路2
1へ送る。
Next, the valves 29 to 32 are opened, the circulation device 23 such as a blower is driven, and an inert gas such as argon is supplied from the gas supply source 22 such as a gas cylinder to the hot gas passage 2.
Send to 1.

【0049】すると、アルゴンなどの不活性ガスは、加
熱装置24により加熱された後、ホットガス供給口19
から液体金属排出管14へ入り、液体金属18の流通経
路を逆流する。
Then, the inert gas such as argon is heated by the heating device 24 and then heated by the hot gas supply port 19
Enters the liquid metal discharge pipe 14 and flows backward in the flow path of the liquid metal 18.

【0050】即ち、液体金属排出管14から液体金属槽
6内へ入り、捕集用金網11を通過し、断熱材10と外
壁との間を通り、上部の仕切板2と支持板9との間隙8
を通り、液体金属供給管13へ入って、ホットガス排出
口20からホットガス流路21へ戻される。
That is, the liquid metal discharge pipe 14 enters the liquid metal tank 6, passes through the collecting wire net 11, passes between the heat insulating material 10 and the outer wall, and the upper partition plate 2 and the support plate 9 are connected. Gap 8
After passing through, the liquid metal is supplied to the liquid metal supply pipe 13 and returned from the hot gas discharge port 20 to the hot gas passage 21.

【0051】以後、アルゴンなどの不活性ガスは、ブロ
ワなどの循環装置23により、ホットガス供給口19へ
送られて、上記経路を循環する。
Thereafter, an inert gas such as argon is sent to the hot gas supply port 19 by the circulation device 23 such as a blower and circulates in the above path.

【0052】又、アルゴンなどの不活性ガスが循環され
るようになったら、弁32を閉じて、ガス供給源22か
らの不活性ガスの供給を停止する。
When the inert gas such as argon is circulated, the valve 32 is closed and the supply of the inert gas from the gas supply source 22 is stopped.

【0053】このように、不活性ガスを加熱して、液体
金属18の流通経路を逆流させることにより、捕集用金
網11の目を詰まらせていた不純物を含む液体金属18
分が溶け出して下部の仕切板3上に流下し、下部の仕切
板3から排液管25を介して排液タンク26へ排出され
る。
In this manner, the inert gas is heated to cause the liquid metal 18 to flow backward, so that the liquid metal 18 containing impurities that has clogged the collecting wire net 11 is blocked.
The fraction melts and flows down onto the lower partition plate 3, and is discharged from the lower partition plate 3 to the drain tank 26 via the drain pipe 25.

【0054】これによって、捕集用金網11の目詰まり
が解消され、液体金属純化装置の機能が回復される。
As a result, the clogging of the collecting wire net 11 is eliminated and the function of the liquid metal purifying device is restored.

【0055】液体金属純化装置の機能が回復されたら、
上記のようにして、液体金属純化装置の運転を再開し、
液体金属18から不純物を除去する。
Once the function of the liquid metal purifier is restored,
As described above, restart the operation of the liquid metal purifier,
Impurities are removed from the liquid metal 18.

【0056】尚、本発明は、上述の実施例にのみ限定さ
れるものではなく、ホットガス流路21は循環流路とせ
ずに開放流路としても良いこと、その他、本発明の要旨
を逸脱しない範囲内において種々変更を加え得ることは
勿論である。
The present invention is not limited to the above-mentioned embodiment, and the hot gas passage 21 may be an open passage instead of the circulation passage, and other deviates from the gist of the present invention. It goes without saying that various changes can be made within the range not covered.

【0057】[0057]

【発明の効果】以上説明したように、本発明の液体金属
純化装置によれば、不純物捕集装置の目詰まりを除去し
て、機能回復を図ることができるという優れた効果を奏
し得る。
As described above, according to the liquid metal purifying apparatus of the present invention, the excellent effect that the clogging of the impurity trapping device can be removed and the function can be recovered can be obtained.

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

【図1】本発明の一実施例の概略側方断面図である。FIG. 1 is a schematic side sectional view of an embodiment of the present invention.

【図2】図1の装置の目詰まりを解消する場合の作動図
である。
FIG. 2 is an operation diagram when the clogging of the apparatus of FIG. 1 is cleared.

【図3】従来例の概略側方断面図である。FIG. 3 is a schematic side sectional view of a conventional example.

【符号の説明】[Explanation of symbols]

6 液体金属槽 11 不純物捕集装置(捕集用金網) 13 液体金属供給管 14 液体金属排出管 18 液体金属 19 ホットガス供給口 20 ホットガス排出口 21 ホットガス流路 22 ガス供給源 23 循環装置 24 加熱装置 26 排液タンク 27,28 弁 33 降温装置 6 Liquid Metal Tank 11 Impurity Collection Device (Collection Wire Mesh) 13 Liquid Metal Supply Pipe 14 Liquid Metal Discharge Pipe 18 Liquid Metal 19 Hot Gas Supply Port 20 Hot Gas Discharge Port 21 Hot Gas Flow Path 22 Gas Supply Source 23 Circulation Device 24 heating device 26 drainage tank 27, 28 valve 33 temperature lowering device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 液体金属供給管と液体金属排出管を接続
された液体金属槽の内部に降温装置と不純物捕集装置を
配置された液体金属純化装置において、液体金属供給管
と液体金属排出管に液体金属の給排を停止させる弁を設
けると共に、液体金属供給管と液体金属排出管に、液体
金属槽内部に対して加熱されたガスを液体金属とは逆方
向に流すホットガス排出口とホットガス供給口をそれぞ
れ形成し、更に、液体金属槽に排液タンクを接続したこ
とを特徴とする液体金属純化装置。
1. A liquid metal purifying apparatus in which a temperature lowering device and an impurity collecting device are arranged inside a liquid metal tank connected to a liquid metal supply pipe and a liquid metal discharge pipe, wherein the liquid metal supply pipe and the liquid metal discharge pipe are provided. A valve for stopping the supply and discharge of liquid metal is provided in the liquid metal supply pipe and the liquid metal discharge pipe, and a hot gas discharge port for flowing the gas heated inside the liquid metal tank in the opposite direction to the liquid metal. A liquid metal purifying apparatus, characterized in that hot gas supply ports are formed respectively, and a drainage tank is connected to the liquid metal tank.
【請求項2】 ホットガス排出口とホットガス供給口の
間をホットガス流路で接続し、ホットガス流路の途中に
ガス供給源と循環装置と加熱装置を設けた請求項1記載
の液体金属純化装置。
2. The liquid according to claim 1, wherein the hot gas discharge port and the hot gas supply port are connected by a hot gas passage, and a gas supply source, a circulation device and a heating device are provided in the middle of the hot gas passage. Metal purifier.
JP6241335A 1994-10-05 1994-10-05 Liquid metal purification device Pending JPH08105997A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6241335A JPH08105997A (en) 1994-10-05 1994-10-05 Liquid metal purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6241335A JPH08105997A (en) 1994-10-05 1994-10-05 Liquid metal purification device

Publications (1)

Publication Number Publication Date
JPH08105997A true JPH08105997A (en) 1996-04-23

Family

ID=17072776

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6241335A Pending JPH08105997A (en) 1994-10-05 1994-10-05 Liquid metal purification device

Country Status (1)

Country Link
JP (1) JPH08105997A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109859868A (en) * 2019-01-10 2019-06-07 中国原子能科学研究院 A kind of high temperature lithium circuit purification hot trap system
CN112349440A (en) * 2020-11-01 2021-02-09 百色学院 Liquid metal purification device and application method thereof
CN113284640A (en) * 2021-05-26 2021-08-20 中国原子能科学研究院 Floating impurity capturing device for reactor

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109859868A (en) * 2019-01-10 2019-06-07 中国原子能科学研究院 A kind of high temperature lithium circuit purification hot trap system
CN109859868B (en) * 2019-01-10 2024-05-10 中国原子能科学研究院 Hot trap system for purifying high-temperature lithium loop
CN112349440A (en) * 2020-11-01 2021-02-09 百色学院 Liquid metal purification device and application method thereof
CN112349440B (en) * 2020-11-01 2022-10-18 百色学院 Liquid metal purification device and application method thereof
CN113284640A (en) * 2021-05-26 2021-08-20 中国原子能科学研究院 Floating impurity capturing device for reactor
CN113284640B (en) * 2021-05-26 2024-09-27 中国原子能科学研究院 Floating impurity capturing device for reactor

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