JPS60149801A - Pre-treatment method on inspection of high-temperature liquid metal treating apparatus - Google Patents
Pre-treatment method on inspection of high-temperature liquid metal treating apparatusInfo
- Publication number
- JPS60149801A JPS60149801A JP361484A JP361484A JPS60149801A JP S60149801 A JPS60149801 A JP S60149801A JP 361484 A JP361484 A JP 361484A JP 361484 A JP361484 A JP 361484A JP S60149801 A JPS60149801 A JP S60149801A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- gas
- liquid metal
- temperature liquid
- sodium
- 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.)
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- Investigating And Analyzing Materials By Characteristic Methods (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は高温液体金属取扱機器の点検時の前処理方法に
関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a pretreatment method for inspecting high-temperature liquid metal handling equipment.
高温液体金属取扱機器の1つにシェルアンドチューブ型
熱交換器がある。同シェルアンドチューブ型熱交換器の
従来例を第1図により説明すると、(1)がシェルアン
ドチューブ型熱交換器の胴、(2)示ナトリウム入口配
管、(3)がナトリウム出口ノズル、(4)が水・蒸気
入口ヘッダ、(5)が下降管、(6)が同下降管(5)
とヘリカルコイル伝熱管とをつなぐつなぎ部、(7)が
ヘリカルコイル伝熱部、(8)が上昇管、(9)が蒸気
出口ヘッダ、(11が蒸気系配管、(1])が水・蒸気
系配管、叫が放出系ノズル、(13)が外側円筒シュラ
ウド、<14)が内側円筒シュラウド、(15)(1,
6)が管板で、炉心で加熱された高温す) IJウム(
高温液体金属)がナトリウム入口配管(2)からシェル
アンドチューブ型熱交換器内へ導入されて、ヘリカルコ
イル伝熱部(7)へ導かれる。ここで水側(伝熱管内)
と熱交換を行ないながら下降し、最終的にはす) IJ
ウム出ロノズル(3)からシェルアンドチューブ型熱交
換器外へ導出される。一方、上記水側は、水・蒸気入口
ヘッダ(4)から管板(へ)により各伝熱管に分けられ
、まず、下降管(5)により外側シュラウド”(131
と胴(1)との間を下降し、下端に達した後、下降管(
5)とヘリカルコイル管とのつなぎ部(6)を経てヘリ
カルコイル伝熱部(7)に至る。−このヘリカルコイル
伝熱部(力でナトリウム側(胴側−管外)と熱交換を行
ない、上昇管(8)を経て蒸気出口ヘッダ(9)に集め
られて、タービン系へ導かれるようになっている。One type of high-temperature liquid metal handling equipment is a shell-and-tube heat exchanger. A conventional example of the shell-and-tube heat exchanger is explained with reference to FIG. 1. (1) shows the body of the shell-and-tube heat exchanger, (2) shows the sodium inlet pipe, (3) shows the sodium outlet nozzle, and (3) shows the sodium outlet nozzle. 4) is the water/steam inlet header, (5) is the downcomer pipe, and (6) is the downcomer pipe (5).
and the helical coil heat transfer tube, (7) is the helical coil heat transfer section, (8) is the riser tube, (9) is the steam outlet header, (11 is the steam system piping, (1) is the water Steam system piping, (13) is the discharge system nozzle, (13) is the outer cylindrical shroud, <14) is the inner cylindrical shroud, (15) (1,
6) is the tube plate, which is heated at high temperature in the reactor core) IJum (
High temperature liquid metal) is introduced into the shell-and-tube heat exchanger from the sodium inlet pipe (2) and guided to the helical coil heat transfer section (7). Here, the water side (inside the heat transfer tube)
(IJ descends while exchanging heat with IJ)
It is led out of the shell-and-tube type heat exchanger through the nozzle (3). On the other hand, the water side is divided into heat exchanger tubes from the water/steam inlet header (4) to the tube plate, and first, the outer shroud (131
and the shell (1), and after reaching the lower end, the downcomer pipe (
5) and the helical coil tube through the connecting part (6) to reach the helical coil heat transfer part (7). - This helical coil heat transfer section (power exchanges heat with the sodium side (shell side - outside the tube), and the steam is collected in the steam outlet header (9) via the riser pipe (8) and guided to the turbine system. It has become.
上記のように液体金属冷却型高速増殖炉のシェルアンド
チューブ型熱交換器は、内部に液体金属をもち、これで
熱の授受を行なっている。液体金属としては、ナトリウ
ムの外に、カリウム、またはナトリウムとカリウムとの
合金のように非常に反応性に富むものも使用され、通常
運転時には、これらの液体金属をもつ空間が完全に外気
にふれないようにカバーガスにより密封、遮断されてい
るが、メンテナンスや事故時には、機器を開けて、内部
の構造物を点検したり、交換する必要があり、その作業
を従来は次の手順で行なっていた。以下、ナトリウムで
説明すると、まずナトリウムを、メンテナンスする必要
のある機器内から排出し、次いです) IJウム温度を
下げ、内部構造物の外表面に付着しているナトリウムを
固化させ、次いでこの機器内に付着しているナトリウム
の外表面をカバーする安定化ガスを導入する。なおここ
で外表面をカバーするとは、例えば炭酸ガス(CO2ま
たはCO)や酸素02を導入して、ナトリウムの表面に
、空気にふれても反応しない物質(Na2CO3,Na
2O。As mentioned above, the shell-and-tube heat exchanger of a liquid metal-cooled fast breeder reactor has liquid metal inside, which transfers heat. In addition to sodium, highly reactive liquid metals such as potassium or an alloy of sodium and potassium are also used as liquid metals, and during normal operation, the space containing these liquid metals is completely exposed to outside air. However, in the event of maintenance or an accident, it is necessary to open the equipment and inspect or replace the internal structure. Conventionally, this work was performed using the following steps. Ta. In the following explanation using sodium, first the sodium is discharged from the equipment that requires maintenance, then the temperature is lowered to solidify the sodium adhering to the outer surface of the internal structure, and then this Introduce a stabilizing gas that covers the outer surface of the sodium adhering to the inside of the device. Note that covering the outer surface here means, for example, introducing carbon dioxide gas (CO2 or CO) or oxygen 02 to cover the surface of sodium with substances that do not react even when exposed to air (Na2CO3, Na2CO3,
2O.
その他)を作ることである。この外気にふれても問題の
ない層を作った後に、内部構造物を外に取り出して、必
要な作業を行なう。上記のように内部構造物の外表面に
付着しているナトリウムの表面をカバーする安定化ガス
を導入する場合、特に温度をコントロールせずになりゆ
きの温度で行なっていた。このため、機器内にあるカバ
ーガス(不活性ガス、例えばA’r)と混合して、内部
機器の表面全体に十分にゆき渡らない。またゆき渡るに
しても多くの時間を要するという問題があった。and others). After creating a layer that does not cause any problems even when exposed to the outside air, the internal structure is taken out and the necessary work is carried out. When introducing a stabilizing gas to cover the surface of the sodium adhering to the outer surface of the internal structure as described above, the temperature was not particularly controlled and was carried out at the natural temperature. For this reason, it does not mix with the cover gas (inert gas, eg A'r) inside the device and is not sufficiently distributed over the entire surface of the internal device. There was also the problem that it took a lot of time to cross.
この点を、ヘリカルコイル伝熱部(力に対する作業に例
をとってさらに説明すると、ヘリカルコイル伝熱部(力
を何らかの原因で外に取り出して検査したい場合には、
まずループをドレンすることにより、内部にあるナトリ
ウムを排出し次いで温度をナトリウム固化温度以下に下
げ、次いで内部機器表面に付着しているナトリウム表面
をカバー(固定化)する安定化ガスをカバーガス系(国
から内部へ導入する。このとき、導入される安定化ガス
の温度は特にコントロールされておらず、なりゆきにま
かされており、上述のように内部にある不活性ガス(A
r)と混合して、構造の複雑に入りくんでいるヘリカル
コイル伝熱部(7)の表面全体に十分にゆき渡らない。To further explain this point using an example of working with force on a helical coil heat transfer section (helical coil heat transfer section),
First, by draining the loop, the sodium inside is discharged, and then the temperature is lowered below the sodium solidification temperature, and then stabilizing gas is introduced into the cover gas system to cover (immobilize) the sodium surface adhering to the internal equipment surface. (Introduced from the country into the interior. At this time, the temperature of the stabilizing gas introduced is not particularly controlled and is left to its own discretion. As mentioned above, the temperature of the stabilizing gas inside is
r) and does not sufficiently spread over the entire surface of the helical coil heat transfer section (7), which has a complex structure.
またゆき渡るにしても多くの時間を要するという問題が
あった。There was also the problem that it took a lot of time to cross.
本発明は前記の問題点に対処・するもので、高温の液体
アルカリ金属を受け入れてその自由液面上にカバーガス
空間部の形成される高温液体金属取扱機器の内部点検に
先だち、内部の液体アルカリ金属を排出し、カバーガス
と比重の異なる安定化ガスを内部−導入してカバーガス
を排出することを特徴とした高温液体金属取扱機器の点
検時の前処理方法に係り、その目的とする処は、導入し
た安定化ガスを機器内部の、例えば構造が複雑に入りく
んだヘリカルコイル伝熱部等にも迅速に、十分にゆき渡
らせることができて、その表面に付着している液体アル
カリ金属の表面を安定化させることができる高温液体金
属取扱機器の点検時の前処理方法を供する点にある。The present invention addresses and solves the above-mentioned problems.Prior to internal inspection of high-temperature liquid metal handling equipment that receives high-temperature liquid alkali metal and has a cover gas space above the free liquid level, The purpose of this invention relates to a pretreatment method for inspecting high-temperature liquid metal handling equipment, which is characterized by discharging alkali metals, introducing a stabilizing gas with a different specific gravity from the cover gas, and discharging the cover gas. The stabilizing gas introduced into the device can be quickly and sufficiently distributed inside the device, such as the helical coil heat transfer part, which has a complex structure, and the liquid adhering to the surface can be quickly and sufficiently distributed. The present invention provides a pretreatment method for inspecting high-temperature liquid metal handling equipment that can stabilize the surface of alkali metals.
次に本発明の高温液体金属取扱機器の点検時の前処理方
法を第2,3図に示す実施例により説明すると、(1)
がシェルアンドチューブ型熱交換器の胴、(2)がナト
リウム入口配管、(3)がナトリウム出口ノズル、(力
がヘリカルコイル伝熱部、0国が外側円筒シュラウド、
(1勾が内側円筒シュラウド、(11が安定化ガス供給
系、(2(llが同安定化ガス供給系(11の温度調節
機器(冷却器または加熱器) 、 +211が止め弁で
、安定化ガスの温度を機器内部にあるガス(Ar )の
温度よりも高くするか、低くするかして、導入する安定
化ガスと機器内部にあるカバーガスとの間に比重の異な
る境界層を生じさせるために、導入する安定化ガスの温
度をコントロールして機器内部へ導入する温度調節機器
(瀾を安定化ガス供給系α1に設けている。なお始めか
ら高温または低温になっている安定化ガスを導入する場
合には、温度調節機器(イ)を必要としない。また安定
イピガスの温度を機器内部で制御することも可能である
。Next, the pretreatment method for inspection of high-temperature liquid metal handling equipment according to the present invention will be explained with reference to the embodiment shown in Figs. 2 and 3. (1)
is the shell of the shell-and-tube heat exchanger, (2) is the sodium inlet pipe, (3) is the sodium outlet nozzle, (force is the helical coil heat transfer part, zero country is the outer cylindrical shroud,
(1 is the inner cylindrical shroud, (11 is the stabilizing gas supply system, (2 is the stabilizing gas supply system (11 is the temperature control device (cooler or heater), +211 is the stop valve, and is the stabilizing gas supply system. By making the gas temperature higher or lower than the temperature of the gas (Ar) inside the device, a boundary layer with a different specific gravity is created between the stabilizing gas to be introduced and the cover gas inside the device. In order to control the temperature of the stabilizing gas introduced into the equipment, a temperature regulating device (a condenser) is installed in the stabilizing gas supply system α1. In the case of introduction, a temperature control device (a) is not required.It is also possible to control the temperature of stable Ipigas inside the device.
高温液体金属取扱機器(例えばシェルアンドチューブ型
熱交換器)は高温の液体アルカリ金属(ナトリウム、カ
リウム、ナトリウムとカリウムとの合金など)を受け入
れて、その自由液面上にカバーガス空間部が形成されて
いる。この高温液体金属取扱機器の内部を点検する場合
、それに先だって、内部のアルカリ金属を排出し、次い
でカバーガスと比重の異なる所定温度の安定化ガスを安
定化ガス供給系(I9から内部へ導入して、カバーガス
を排出し、両ガスの間に後述の密度差を生じさせて、ガ
スの混合を抑える。第2.6図は、低温の安定化ガスを
導入した場合で、導入した安定化ガスは比重が重くて、
ヘリカルコイル伝熱部(力の各伝熱管の間を下から上へ
万遍なく上昇してゆく。High-temperature liquid metal handling equipment (e.g. shell-and-tube heat exchangers) accepts high-temperature liquid alkali metals (sodium, potassium, alloys of sodium and potassium, etc.), and a cover gas space is formed above the free liquid surface. has been done. When inspecting the inside of this high-temperature liquid metal handling equipment, first discharge the alkali metal inside, then introduce a stabilizing gas at a predetermined temperature with a specific gravity different from that of the cover gas into the inside from the stabilizing gas supply system (I9). Then, the cover gas is discharged, creating a density difference between the two gases as described below, and suppressing the mixing of the gases.Figure 2.6 shows the case where a low-temperature stabilizing gas is introduced. Gas has a heavy specific gravity,
Helical coil heat transfer section (force rises evenly from bottom to top between each heat transfer tube.
一方、カバーガスは胴(1)の上部に設けられたガス排
出系から胴(1)外へ排出されて、カバーガスと安定化
ガスとが大きく混合することがない。以上は低温の安定
化ガスを導入する場合であるが、高温の安定化ガスを導
入する場合も同じで、機器内上部から導入した安定化ガ
スは、機器内にあるカバーガスを上から下へ押し下げて
、機器内に充満してゆく。但しこの場合には、ガス排出
系が胴(1)の底部に設けられており、低温のカバーガ
スがこの排出系から胴(1)外へ排出される。なおりバ
ーガスと安定化ガスとの比重(密度)差は、両ガスの種
類により異なるが、代表的な例を挙げると次の通りであ
る。(1)カッミーガスがArで、安定化ガスがCO2
の場合、機器内にあるカバーガスArはその温度が50
Cであれば比重が1.511.<gl&、導入する安定
化ガスCO2はその温度が20Cであれば比重が1.8
4に9/nl”で、両ガスの比重差は、0.33kg/
rr?である。なおこの場合、機器を多少暖めて、上記
温度程度の安定化ガスを導入するとよい。(II)カバ
ーガスがArで、安定化ガスが02の場合、機器内にあ
るカバーガスArはその温度が80cであれば比重が1
.66kg/rIIs、導入する安定化ガス02はその
温度が5 DCであれば比重が1.21に!?/rrl
’で、両ガスの比重差は、0.45 kl?/ rn’
である。なおこの場合、導入する安定化ガス02の温度
をあげてやるとよい。On the other hand, the cover gas is discharged to the outside of the shell (1) from a gas exhaust system provided at the upper part of the shell (1), so that the cover gas and the stabilizing gas do not mix significantly. The above is for introducing a low-temperature stabilizing gas, but the same applies when introducing a high-temperature stabilizing gas.The stabilizing gas introduced from the top of the device passes through the cover gas inside the device from top to bottom. Push it down and it will fill the device. However, in this case, a gas exhaust system is provided at the bottom of the shell (1), and the low-temperature cover gas is discharged from this exhaust system to the outside of the shell (1). The difference in specific gravity (density) between the Naori bar gas and the stabilizing gas varies depending on the type of both gases, but typical examples are as follows. (1) Cumming gas is Ar and stabilizing gas is CO2
In this case, the cover gas Ar in the equipment has a temperature of 50
If it is C, the specific gravity is 1.511. <gl&, if the temperature of the introduced stabilizing gas CO2 is 20C, the specific gravity is 1.8
4 to 9/nl", and the difference in specific gravity between the two gases is 0.33 kg/nl.
rr? It is. In this case, it is preferable to warm up the device a little and introduce stabilizing gas at about the above temperature. (II) When the cover gas is Ar and the stabilizing gas is 02, the cover gas Ar in the device has a specific gravity of 1 if its temperature is 80c.
.. 66 kg/rIIs, the introduced stabilizing gas 02 has a specific gravity of 1.21 if its temperature is 5 DC! ? /rrl
'Then, the difference in specific gravity between both gases is 0.45 kl? /rn'
It is. In this case, it is preferable to raise the temperature of the stabilizing gas 02 to be introduced.
本発明の高温液体金属取扱機器の点検時の前処理方法は
前記のように高温の液体アルカリ金属を受け入れてその
自由液面上にカバーガス空間部の形成される高温液体金
属取扱機器の内部点検に先だち、内部の液体アルカリ金
属を排出し、カバーガスと比重の異なる安定化ガスを内
部へ導入してカバーガスを排出するようにしており、導
入した安定化ガスを機器内部の、例えば構造の複雑に入
りくんだヘリカルコイル伝熱部等にも迅速に、十分にゆ
き渡らせることができて、その表面に付着している液体
アルカリ金属の表面を安定化させることができる効果が
ある。The pretreatment method for inspection of high-temperature liquid metal handling equipment according to the present invention is, as described above, for internal inspection of high-temperature liquid metal handling equipment in which a high-temperature liquid alkali metal is received and a cover gas space is formed above the free liquid surface. Prior to this, the liquid alkali metal inside is discharged, and a stabilizing gas with a specific gravity different from that of the cover gas is introduced into the interior, and the cover gas is discharged. It has the effect of being able to quickly and sufficiently spread the heat to a complex helical coil heat transfer section, etc., and stabilizing the surface of the liquid alkali metal adhering to the surface.
以上本発明を実施例について説明したが、勿論本発明は
このような実施例にだけ局限されるものではなく、本発
明の精神を逸脱しない範囲内で種々の設計の改変を施し
うるものである。Although the present invention has been described above with reference to embodiments, it goes without saying that the present invention is not limited to such embodiments, and that various design modifications can be made without departing from the spirit of the present invention. .
第1図は高温液体金属取扱機器を示す縦断側面図、第2
図は本発明に係る高温液体金属取扱機器の点検時の前処
理方法の一実施例を示す説明図、第3図はその拡大説明
図である。
(1)〜(161・・・高温液体金属取扱機器(シェル
アンドチューブ型熱交換器)、翰・・・安定化ガス供給
系。
復代理人 弁理士 岡 本 重 窯
外3名
第1図Figure 1 is a vertical cross-sectional side view showing high-temperature liquid metal handling equipment, Figure 2
The figure is an explanatory diagram showing one embodiment of the pretreatment method for inspection of high-temperature liquid metal handling equipment according to the present invention, and FIG. 3 is an enlarged explanatory diagram thereof. (1) - (161... High-temperature liquid metal handling equipment (shell and tube type heat exchanger), Kanji... Stabilizing gas supply system. Sub-agent: Patent attorney Shige Okamoto, 3 people outside the kiln Figure 1
Claims (1)
カバーガス空間部の形成される高温液体金属取扱機器の
内部点検に先だち、内部の液体アルカリ金属を排出し、
カバーガスと比重の異なる安定化ガスを内部へ導入して
カバーガスを排出することを特徴とした高温液体金属取
扱機器の点検時の前処理方法。Prior to internal inspection of high-temperature liquid metal handling equipment that receives high-temperature liquid alkali metal and forms a cover gas space above the free liquid surface, the internal liquid alkali metal is discharged,
A pretreatment method for inspecting high-temperature liquid metal handling equipment characterized by introducing a stabilizing gas with a different specific gravity from the cover gas into the interior and discharging the cover gas.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP361484A JPS60149801A (en) | 1984-01-13 | 1984-01-13 | Pre-treatment method on inspection of high-temperature liquid metal treating apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP361484A JPS60149801A (en) | 1984-01-13 | 1984-01-13 | Pre-treatment method on inspection of high-temperature liquid metal treating apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60149801A true JPS60149801A (en) | 1985-08-07 |
Family
ID=11562364
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP361484A Pending JPS60149801A (en) | 1984-01-13 | 1984-01-13 | Pre-treatment method on inspection of high-temperature liquid metal treating apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60149801A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014513260A (en) * | 2011-03-11 | 2014-05-29 | ステレンボッシュ ユニバーシティ | Particularly suitable for heat storage equipment |
-
1984
- 1984-01-13 JP JP361484A patent/JPS60149801A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014513260A (en) * | 2011-03-11 | 2014-05-29 | ステレンボッシュ ユニバーシティ | Particularly suitable for heat storage equipment |
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