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JPS5925452B2 - Hydrogen concentration measurement device in liquid metal - Google Patents
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JPS5925452B2 - Hydrogen concentration measurement device in liquid metal - Google Patents

Hydrogen concentration measurement device in liquid metal

Info

Publication number
JPS5925452B2
JPS5925452B2 JP52111391A JP11139177A JPS5925452B2 JP S5925452 B2 JPS5925452 B2 JP S5925452B2 JP 52111391 A JP52111391 A JP 52111391A JP 11139177 A JP11139177 A JP 11139177A JP S5925452 B2 JPS5925452 B2 JP S5925452B2
Authority
JP
Japan
Prior art keywords
hydrogen
gas
diffusion membrane
sodium
liquid metal
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.)
Expired
Application number
JP52111391A
Other languages
Japanese (ja)
Other versions
JPS5445197A (en
Inventor
敏雄 舟田
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.)
Doryokuro Kakunenryo Kaihatsu Jigyodan
Original Assignee
Doryokuro Kakunenryo Kaihatsu Jigyodan
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 Doryokuro Kakunenryo Kaihatsu Jigyodan filed Critical Doryokuro Kakunenryo Kaihatsu Jigyodan
Priority to JP52111391A priority Critical patent/JPS5925452B2/en
Publication of JPS5445197A publication Critical patent/JPS5445197A/en
Publication of JPS5925452B2 publication Critical patent/JPS5925452B2/en
Expired 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

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  • Investigating And Analyzing Materials By Characteristic Methods (AREA)
  • Monitoring And Testing Of Nuclear Reactors (AREA)

Description

【発明の詳細な説明】 本発明は、例えは液体ナトリウム等の液体金属中の水素
濃度を測定する装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for measuring hydrogen concentration in a liquid metal, such as liquid sodium.

液体金属、特に液体ナトリウムは、高速増殖炉等の冷却
材として使用されており、その中の水素濃度を測定する
装置は、例えば蒸気発生器部でのナトリウム−水反応を
早期に検出するリーク検出器としても重要である。従来
の水素計は、ニッケル等からなるベロー型あるいは半球
型の薄い拡散膜を通して液体金属から拡散透過してくる
水素を、隔離弁を介して接続されたイオンポンプ、また
は真空計や質量分析器などの出力で測定するものである
Liquid metals, especially liquid sodium, are used as coolants in fast breeder reactors, etc., and devices that measure the hydrogen concentration in them are used for leak detection to detect sodium-water reactions at an early stage, for example in steam generators. It is also important as a vessel. Conventional hydrogen meters collect hydrogen that diffuses and permeates from liquid metal through a thin bellows or hemispherical diffusion membrane made of nickel, etc., using an ion pump connected via an isolation valve, a vacuum gauge, a mass spectrometer, etc. It is measured by the output of

測定方法は、例えば、拡散膜の外側に500〜700℃
の液体ナトリウムを流し、内側をイオンポンプで高真空
にし、該拡散膜を透過してくろ水素を、隔離弁を開け該
イオンポンプを作動させながら、あるいは隔離弁を閉じ
前記拡散膜を透過してくろ水素を平衡させ、真空計、質
量分析器、あるいはイオンポンプの出力で水素分圧を測
定することによつてなされろ。しかしながら、このよう
な従来の水素計には次のような問題点がある。0)水素
の吸い過ぎによりイオンポンプが経時変化を起こすこと
、回 水素分圧測定部(室温)と拡散膜部(500〜7
00’C )との温度差による水素分圧の補正が必要な
こと、および、それらの温度が変動すること測定精度が
低下すること、(→ 真空計出力は測定するガスの種類
に依存するため、水素に対する補正が必要であること、
目 真空計自体に水素排気効果があるため、低水素濃度
の測定精度が悪化すること、… 真空壁からのガス放出
、あるいは外部からのリークの問題、Θ 拡散膜は水素
の透過量をできるだけ大きくするため、薄くかつ広い面
積を必要とするが、内部が高真空状態となつているから
該拡散膜には常にナトリウム側か一ら1気圧以上の圧力
がかかつていて、しかも高温で長時間ナトリウムにさら
されるから、拡散膜の機械的強度並びに耐久性の点で問
題があつたこと、等であろ。
For example, the measurement method is to
of liquid sodium is poured into the membrane, the inside is made into a high vacuum using an ion pump, and hydrogen is passed through the diffusion membrane, either by opening the isolation valve and operating the ion pump, or by closing the isolation valve and passing through the diffusion membrane. This can be done by equilibrating the chlorohydrogen and measuring the hydrogen partial pressure with a vacuum gauge, mass spectrometer, or ion pump output. However, such conventional hydrogen meters have the following problems. 0) The ion pump may change over time due to excessive absorption of hydrogen.
It is necessary to correct the hydrogen partial pressure due to the temperature difference from 00'C), and measurement accuracy decreases due to fluctuations in these temperatures. (→ Because the vacuum gauge output depends on the type of gas being measured. , correction for hydrogen is required;
2) The vacuum gauge itself has a hydrogen exhaust effect, which deteriorates the measurement accuracy of low hydrogen concentrations,... Problems with gas release from the vacuum wall or leaks from the outside, Θ The diffusion membrane increases the amount of hydrogen permeation as much as possible. Therefore, it requires a thin and wide area, but since the interior is in a high vacuum state, the diffusion membrane is always under pressure of 1 atm or more from the sodium side, and moreover, the diffusion membrane is exposed to sodium for a long time at high temperatures. This may be due to problems with the mechanical strength and durability of the diffusion membrane due to exposure to water.

このように、従来型の水素計には、解決すべき問題点が
多く、実用性に乏しいものであつた。本発明は、上記の
ような従来技術における種々の問題点をふまえてなされ
たものであつて、その目的とするところは、簡単な構成
で耐久性に優れ、高精度で液体金属中の水素濃度の測定
が可能な装置を提供することにある。
As described above, conventional hydrogen meters have many problems that need to be solved and are not practical. The present invention has been made in view of the various problems in the prior art as described above, and its purpose is to have a simple structure, excellent durability, and highly accurate determination of the hydrogen concentration in liquid metal. The objective is to provide a device capable of measuring.

かかる目的を達成するため、本発明では拡散膜として従
来の半球型、ベロ一型に代えて薄肉細管型、好ましくは
コイル状にした薄肉管型とし、更に、従来の水素計では
拡散膜内側を真空にし、真空内に拡散する水素分圧を測
定していたのに対し、本発明では拡散膜内部に窒素、ア
ルゴン等の不活性ガスを導入し、この不活性ガス中に拡
散する水素を導入した不活性ガスと共にガスクロマトグ
ラフ等のガス分析器に導き、不活性ガス中に含まれてい
る水素の絶対量(モル数)を測定するものである。
In order to achieve this object, the present invention uses a thin-walled tube type, preferably a thin-walled coiled tube type, as the diffusion membrane instead of the conventional hemispherical or tongue-shaped type, and furthermore, in the conventional hydrogen meter, the inside of the diffusion membrane is Whereas a vacuum was created and the partial pressure of hydrogen diffused in the vacuum was measured, the present invention introduces an inert gas such as nitrogen or argon into the diffusion membrane, and introduces hydrogen that diffuses into this inert gas. The inert gas is introduced into a gas analyzer such as a gas chromatograph, and the absolute amount (number of moles) of hydrogen contained in the inert gas is measured.

即ち本発明は、液体金属中に受漬される金属細管状の拡
散膜と、その入口部に第1の開閉弁を介して接続された
不活性キヤリアガス供給部と、前記拡散膜細管の出口部
に第2の開閉弁を介して接続されたガス分析器と、第3
の開閉弁を備え、前記不活性キヤリアガス供給部出口側
とガス分析器入口側とを相互連結するバイパス管と、前
記ガス分析器に付設される既知量の水素を含む標準ガス
容器とを具備し、前記拡散膜を拡散透過してくる水素を
不活性キヤリアガスと共にガス分析器に導き不活性ガス
中の水素量を定量するようにした液体金属中の水素濃度
測定装置である。以下図面に基づき本発明の一実施例に
ついて詳述する。
That is, the present invention provides a diffusion membrane in the form of a metal capillary tube immersed in a liquid metal, an inert carrier gas supply section connected to the inlet portion thereof via a first on-off valve, and an outlet portion of the diffusion membrane capillary tube. a gas analyzer connected to the third on-off valve via a second on-off valve;
a bypass pipe interconnecting the outlet side of the inert carrier gas supply section and the inlet side of the gas analyzer, and a standard gas container containing a known amount of hydrogen attached to the gas analyzer. , is an apparatus for measuring hydrogen concentration in a liquid metal, in which the hydrogen diffused and permeated through the diffusion membrane is guided to a gas analyzer together with an inert carrier gas to quantify the amount of hydrogen in the inert gas. An embodiment of the present invention will be described in detail below based on the drawings.

第1図に示すようlこ、水素濃度測定装置は、拡散膜水
素検出部a、ガス導入部b、ガス分析部cからなる。拡
散膜水素検出部aは、液体ナトリウムループの一部に設
けたバイパスライン1中に金属管拡散膜2を取付けてな
る。金属管2は、内径2.0m71L1肉厚0.1mm
のニツケル製で内容積は約15m1であり、コイル状に
巻かれて挿入されている。次に、ガス導入部bは、金属
細管2内に不活性なガス(この実施例では純アルゴンガ
ス)を導入し、拡散透過した水素をガス分析器部cへ導
くためのもので、内径2.0mmの厚肉のステンレス管
および複数のバルブよりなる。つまり、拡散膜金属細管
2の入口部3は、第1の開閉弁4を介してアルゴンガス
供給装置5に接続され、また、拡散膜金属細管2の出口
部6は、第2の開閉弁7を介してガス分析器部Ciこ接
続されている。更に、前記アルゴンガス供給装置5とガ
ス分析器部cとは第3の開閉弁8を備えたバイパス管9
で相互連絡されている。前記拡散膜金属細管2内へのア
ルゴンガスの導入圧力は、該細管2のガスの流動抵抗に
よつて異なるが、ガス分析器部cに15〜25m1/分
でアルゴンガスを導くために必要な圧力、すなわち0.
5〜3.0気圧程度がよい。このキヤリアガスは、液体
金属から拡散する水素をガス分析器に導入するキヤリア
としての役割の他、ガスの圧力を調整することによつて
拡散膜にかかる負荷圧力を軽減する機能をも果たすもの
である。ガス分析器部cは、本実施例では熱伝導度検出
器(TCD)を装着した市販のガスクロマトグラフ10
であつて、アルゴン中に含まれている微量の水素をPF
オーダーで検出可能であり、結果はレコーダ11で記録
されるようになつている。ガスクロマトグラフ10には
、TCDの更正曲線を求めるため、既知量の水素を含む
アルゴン標準ガス容器12が付設されている。標準ガス
の水素含有量は、金属細管2から導入されるアルゴンガ
ス中の水素含有量と同程度、すなわち10〜100PF
1程度がよい。さて、このように構成された水素濃度測
定装置を用いた測定法には二つの方法、平衡法と連続法
とがある。(1)平衡法 第3の開閉弁8を開け、第1、第2の開閉弁4,7を閉
じ、アルゴンガスを金属細管2内に閉じ込める。
As shown in FIG. 1, the hydrogen concentration measuring device consists of a diffusion membrane hydrogen detection section a, a gas introduction section b, and a gas analysis section c. The diffusion membrane hydrogen detection section a is constructed by attaching a metal tube diffusion membrane 2 to a bypass line 1 provided in a part of the liquid sodium loop. Metal tube 2 has an inner diameter of 2.0 m, 71 L, and a wall thickness of 0.1 mm.
It is made of nickel and has an internal volume of about 15 m1, and is inserted into a coil. Next, the gas introduction part b is for introducing an inert gas (in this example, pure argon gas) into the metal capillary tube 2 and guiding the diffused and permeated hydrogen to the gas analyzer part c. Consists of a .0mm thick stainless steel tube and multiple valves. That is, the inlet section 3 of the diffusion membrane metal capillary tube 2 is connected to the argon gas supply device 5 via the first on-off valve 4, and the outlet section 6 of the diffusion membrane metal capillary tube 2 is connected to the second on-off valve 7. The gas analyzer section Ci is connected through the gas analyzer section Ci. Further, the argon gas supply device 5 and the gas analyzer section c are connected to a bypass pipe 9 equipped with a third on-off valve 8.
are mutually connected. The pressure at which argon gas is introduced into the diffusion membrane metal capillary tube 2 varies depending on the gas flow resistance of the capillary tube 2, but it is the pressure required to introduce argon gas into the gas analyzer section c at a rate of 15 to 25 m1/min. pressure, i.e. 0.
Approximately 5 to 3.0 atmospheres is preferable. This carrier gas not only functions as a carrier to introduce hydrogen diffusing from the liquid metal into the gas analyzer, but also functions to reduce the load pressure on the diffusion membrane by adjusting the gas pressure. . In this embodiment, the gas analyzer section c is a commercially available gas chromatograph 10 equipped with a thermal conductivity detector (TCD).
The trace amount of hydrogen contained in argon is PF
Detection is possible by order, and the results are recorded by a recorder 11. The gas chromatograph 10 is equipped with an argon standard gas container 12 containing a known amount of hydrogen in order to obtain a TCD calibration curve. The hydrogen content of the standard gas is about the same as the hydrogen content in the argon gas introduced from the metal capillary tube 2, that is, 10 to 100PF.
About 1 is good. There are two measurement methods using the hydrogen concentration measuring device configured as described above: the equilibrium method and the continuous method. (1) Equilibrium method The third on-off valve 8 is opened, the first and second on-off valves 4 and 7 are closed, and argon gas is confined within the metal capillary tube 2.

一定時間液体ナトリウム中から水素を拡散透過させ、充
分に平衡に達した時点で第3の開閉弁8を閉じ、第1、
第2の開閉弁4,7を開いて細管2内の水素をアルゴン
ガスと共にガスクロマトグラフ10に導き、測定を行う
。次いで各開閉弁4,7,8を元の状態に戻すのである
。第2図はこのようにして求めたアルゴン中の水素濃度
測定結果の一例であり、縦軸はガスクロマトグラフ出力
、横軸は時間を示している。
Hydrogen is diffused and permeated from the liquid sodium for a certain period of time, and when equilibrium is sufficiently reached, the third on-off valve 8 is closed, and the first,
The second on-off valves 4 and 7 are opened to guide hydrogen in the thin tube 2 together with argon gas to the gas chromatograph 10 for measurement. Next, each on-off valve 4, 7, 8 is returned to its original state. FIG. 2 shows an example of the hydrogen concentration measurement results in argon obtained in this way, where the vertical axis shows the gas chromatograph output and the horizontal axis shows time.

曲線A,Bは、コールドトラツプ法によつてナトリウム
中の水素濃度を変えた場合(Aはコールドトラツプの最
低温度が250℃、Bは150℃)に対応する。A,B
各曲線のピーク面積を求めることによつて、アルゴンガ
ス中の水素量(モル数)を求めることができる。理想気
体の場合、次のポール・シヤルルの法則が成立する。
Curves A and B correspond to the case where the hydrogen concentration in sodium is changed by the cold trap method (the lowest cold trap temperature for A is 250°C and for B 150°C). A, B
By determining the peak area of each curve, the amount of hydrogen (number of moles) in the argon gas can be determined. In the case of an ideal gas, the following Paul-Charles law holds.

P=NRT・・・・・・・・・ (1) ここで、Pは金属細管内の水素分圧、 は金属細管内の容積、 nは金属細管内の水素量(モル数)、 Rは気体定数、 Tは金属細管内の絶対温度 である。P=NRT・・・・・・・・・(1) Here, P is the hydrogen partial pressure inside the metal tube, is the volume inside the metal tube, n is the amount of hydrogen in the metal tube (number of moles), R is the gas constant, T is the absolute temperature inside the metal tube It is.

水素量nから金属細管2内の水素分圧、すなわち平衡す
るナトリウム中の水素分圧Pを決定しうる。
From the hydrogen amount n, the hydrogen partial pressure inside the metal capillary 2, that is, the hydrogen partial pressure P in the equilibrium sodium can be determined.

また、ナトリウム中の水素分圧Pは、シーバーツ(Si
everts)の法則によりナトリウム中の水素濃度と
次の関係がある。
In addition, the hydrogen partial pressure P in sodium is Siverts (Si
Everts' law, the following relationship exists between the hydrogen concentration in sodium and the hydrogen concentration in sodium.

ClI−K−′V ・・・・・・・・・(2)ここ
で、CHはナトリウム中の水素濃度、Kはシーバーツ定
数、 Pはナトリウム中の水素分圧、 である。
ClI-K-'V (2) Here, CH is the hydrogen concentration in sodium, K is Sievert's constant, and P is the hydrogen partial pressure in sodium.

上記(1),(2)式から、 となり、ナトリウム中の水素濃度CHを求めることがで
きる。
From the above equations (1) and (2), it becomes as follows, and the hydrogen concentration CH in sodium can be determined.

このようにして求めたナトリウム中の水素濃度(p芦)
とコールドトラツプ温度の関係を、参考のため、第3図
に示す。この平衡測定法では拡散膜細管部2の温度が3
50〜600℃と変動しても、また細管2内のアルゴン
ガス圧を変えても(たとえ真空に引いても)水素濃度測
定値がほとんど変化しない特徴がある。平衡に達するに
必要な時間は細管部のナトリウム温度に依存するが、低
温(350のC)でも数分間で充分であることが判明し
た。かかる測定法は、従来の水素計のような拡散膜部と
測定部との温度差等の補正が不要で、データの解析が極
めて容易なため、ナトリウム中の水素濃度を精度よく検
出するのに適している。測定時間間隔は10分程度あれ
ば充分であり、通常のナトリウム系の水素濃度測定に必
要な頻度を満足するものである。(11)連続法 第1図において、第3図の開閉弁8を閉じ、第1、第2
の開閉弁4,7を開け、常時アルゴンガスを拡散膜金属
細管2に流し、拡散透過してくる水素量を連続的にガス
クロマトグラフ10に導入し、定量する。
Hydrogen concentration in sodium determined in this way (p)
The relationship between cold trap temperature and cold trap temperature is shown in Figure 3 for reference. In this equilibrium measurement method, the temperature of the diffusion membrane tube section 2 is 3
It has the characteristic that the measured value of hydrogen concentration hardly changes even if it fluctuates from 50 to 600°C or even if the argon gas pressure inside the thin tube 2 is changed (even if it is evacuated). The time required to reach equilibrium depends on the sodium temperature in the capillary section, but a few minutes was found to be sufficient even at low temperatures (350 C). This measurement method does not require correction for temperature differences between the diffusion membrane part and the measurement part as in conventional hydrogen meters, and data analysis is extremely easy, so it is useful for accurately detecting the hydrogen concentration in sodium. Are suitable. A measurement time interval of about 10 minutes is sufficient and satisfies the frequency required for normal sodium-based hydrogen concentration measurements. (11) In the continuous method shown in Fig. 1, close the on-off valve 8 shown in Fig. 3, and
The on-off valves 4 and 7 are opened, argon gas is constantly flowed through the diffusion membrane metal capillary tube 2, and the amount of hydrogen diffused and permeated is continuously introduced into the gas chromatograph 10 and quantified.

測定結果の一例を第4図に示す。縦軸はガスクロマトグ
ラフ出力、横軸は時間、または拡散膜温度は350℃で
ある。第4図1こおいて、A,B部は前述したコールド
トラツプ温度250℃および1500Cの水素濃度は対
応している。拡散透過する水素量は、ナトリウム中の水
素濃度に依存するが、拡散膜温度の影響も受けやすい。
従つて、この連続法で精度よくナトリウム中の水素濃度
を定量するためには、拡散膜部のナトリウム温度を一定
に保持すること、および(1)の平衡法をあらかじめ実
施してガスクロマトグラフ出力とナトリウム中水素濃度
の関係式を求めておくことが必要である。この連続測定
法の特徴は、連続的にナトリウム中の水素濃度に対応す
る出力が得られ、ナトリウム水素濃度の変動に対する水
素計の追随が速いことであり、このため実際の液体ナト
リウム系では、例えば原子炉二次系蒸気発生部の破損時
のナトリウム一水反応による水素量の増加を検知する所
謂リーク検出器として有効なものである。また、上記二
つの測定方法、すなわち平衡法と連続法とを併用すれば
、連続的な、かつ高精度での水素濃度測定も可能である
An example of the measurement results is shown in FIG. The vertical axis is the gas chromatograph output, and the horizontal axis is time, or the diffusion membrane temperature is 350°C. In FIG. 4, parts A and B correspond to the hydrogen concentrations at the cold trap temperatures of 250° C. and 1500° C., respectively. The amount of hydrogen that diffuses and permeates depends on the hydrogen concentration in sodium, but is also easily influenced by the diffusion membrane temperature.
Therefore, in order to accurately quantify the hydrogen concentration in sodium using this continuous method, it is necessary to maintain the sodium temperature in the diffusion membrane constant and to perform the equilibrium method in (1) in advance to adjust the gas chromatograph output. It is necessary to find the relational expression for the concentration of hydrogen in sodium. The characteristics of this continuous measurement method are that an output corresponding to the hydrogen concentration in sodium can be obtained continuously, and that the hydrogen meter can quickly follow changes in the sodium hydrogen concentration.For this reason, in actual liquid sodium systems, for example, It is effective as a so-called leak detector that detects an increase in the amount of hydrogen due to a sodium-water reaction when the secondary steam generation part of a nuclear reactor is damaged. Further, by using the above two measurement methods, that is, the equilibrium method and the continuous method, it is possible to measure the hydrogen concentration continuously and with high accuracy.

本発明は、上記のように、拡散膜を微細径の細管状とし
たから、機械的強度が改善され、単位体積当りの拡散膜
面積が大きいため液体金属温度が350のC程度の低温
での使用も可能となり、また、拡゛散膜内部に正圧の不
活性ガスを導入するので、膜9こ加わる圧力は軽減され
、かかる要因が相俟つて耐久性b≦格段に向上し、更に
は拡散膜細管が破損しても液体金属は外部に漏れにくく
、万一漏れてもガス導入部管内で直ちに凝固するため極
めて安全性の高いものが得られる効果がある。
As described above, in the present invention, since the diffusion membrane is made into a tubular shape with a fine diameter, the mechanical strength is improved, and the diffusion membrane area per unit volume is large, so that it can be used at a low liquid metal temperature of about 350 C. In addition, since a positive pressure inert gas is introduced into the interior of the diffusion membrane, the pressure applied to the membrane is reduced, and these factors combine to significantly improve durability b≦. Even if the diffusion membrane capillary is damaged, the liquid metal is unlikely to leak to the outside, and even if it leaks, it will solidify immediately within the gas introduction tube, resulting in an extremely safe product.

また、本発明は、その構成が極めて簡単であつて、高精
度で液体金属中の水素濃度の迎淀可能であり、また測定
条件等に応じ゛C平衡測定法または連続測定法のいずれ
かを適宜選択し得、また両者を併用することも可能であ
る等数々のすぐれた効果を奏しうるものである。
In addition, the present invention has an extremely simple configuration, can control the hydrogen concentration in liquid metal with high accuracy, and can use either the C equilibrium measurement method or the continuous measurement method depending on the measurement conditions. They can be selected as appropriate, or both can be used in combination, resulting in a number of excellent effects.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明に係る水素濃度測定装置の一実施例の概
略説明図、第2図は平衡法による測定結果のーー例を示
す図、第3図はナトリウム中水素濃度の測定データの一
例を示す図、第4図は連続法による測定結果の一例を示
す図である。 1・・・・・・バイパスライン、2・・・・・・拡散膜
金属細管、3・・・・・・入口部、6・・・・・・出口
部、4,7,8・・・・・・開閉弁、5・・・・・・ア
ルゴンガス供給装置、10・・・・・・ガスクロマトグ
ラフ。
Figure 1 is a schematic explanatory diagram of an embodiment of the hydrogen concentration measuring device according to the present invention, Figure 2 is a diagram showing an example of measurement results by the equilibrium method, and Figure 3 is an example of measurement data of hydrogen concentration in sodium. FIG. 4 is a diagram showing an example of measurement results by the continuous method. DESCRIPTION OF SYMBOLS 1... Bypass line, 2... Diffusion membrane metal tube, 3... Inlet part, 6... Outlet part, 4, 7, 8... ...Opening/closing valve, 5...Argon gas supply device, 10...Gas chromatograph.

Claims (1)

【特許請求の範囲】 1 液体金属中に浸漬される金属細管状の拡散膜と、そ
の入口部に第1の開閉弁を介して接続された不活性キャ
リアガス供給部と、前記拡散膜細管の出口部に第2の開
閉弁を介して接続されたガス分析器と、第3の開閉弁を
備え、前記不活性キャリアガス供給部出口側とガス分析
器入口側とを相互連結するバイパス管と、前記ガス分析
器に付設される既知量の水素を含む標準ガス容器とを具
備し、前記拡散膜を拡散透過してくる水素を不活性キャ
リアガスと共にガス分析器に導き不活性ガス中の水素量
を定量するようにした液体金属中の水素濃度測定装置。 2 拡散膜を構成する金属細管をコイル状とした特許請
求の範囲第1項記載の装置。
[Claims] 1. A diffusion membrane in the form of a metal capillary tube immersed in a liquid metal, an inert carrier gas supply section connected to its inlet via a first on-off valve, and a diffusion membrane tube-shaped diffusion membrane immersed in a liquid metal. a gas analyzer connected to the outlet via a second on-off valve; and a bypass pipe that includes a third on-off valve and interconnects the inert carrier gas supply section outlet side and the gas analyzer inlet side. , a standard gas container containing a known amount of hydrogen attached to the gas analyzer, and the hydrogen diffused and permeated through the diffusion membrane is guided to the gas analyzer together with an inert carrier gas, and the hydrogen in the inert gas is A device for measuring the concentration of hydrogen in liquid metal. 2. The device according to claim 1, wherein the metal capillary tube constituting the diffusion membrane is coiled.
JP52111391A 1977-09-16 1977-09-16 Hydrogen concentration measurement device in liquid metal Expired JPS5925452B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52111391A JPS5925452B2 (en) 1977-09-16 1977-09-16 Hydrogen concentration measurement device in liquid metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52111391A JPS5925452B2 (en) 1977-09-16 1977-09-16 Hydrogen concentration measurement device in liquid metal

Publications (2)

Publication Number Publication Date
JPS5445197A JPS5445197A (en) 1979-04-10
JPS5925452B2 true JPS5925452B2 (en) 1984-06-18

Family

ID=14559969

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52111391A Expired JPS5925452B2 (en) 1977-09-16 1977-09-16 Hydrogen concentration measurement device in liquid metal

Country Status (1)

Country Link
JP (1) JPS5925452B2 (en)

Also Published As

Publication number Publication date
JPS5445197A (en) 1979-04-10

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