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JPH0237984B2 - - Google Patents
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JPH0237984B2 - - Google Patents

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Publication number
JPH0237984B2
JPH0237984B2 JP57122386A JP12238682A JPH0237984B2 JP H0237984 B2 JPH0237984 B2 JP H0237984B2 JP 57122386 A JP57122386 A JP 57122386A JP 12238682 A JP12238682 A JP 12238682A JP H0237984 B2 JPH0237984 B2 JP H0237984B2
Authority
JP
Japan
Prior art keywords
inert gas
molten metal
hole
hydrogen
flow path
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 - Lifetime
Application number
JP57122386A
Other languages
Japanese (ja)
Other versions
JPS5912348A (en
Inventor
Shiro Terai
Shiro Sato
Sakae Kato
Masaya Imai
Susumu Inumaru
Masahiro Yoshida
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.)
Sumitomo Light Metal Industries Ltd
Original Assignee
Sumitomo Light Metal Industries Ltd
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 Sumitomo Light Metal Industries Ltd filed Critical Sumitomo Light Metal Industries Ltd
Priority to JP57122386A priority Critical patent/JPS5912348A/en
Priority to GB08300562A priority patent/GB2123957B/en
Priority to DE3303122A priority patent/DE3303122C2/en
Publication of JPS5912348A publication Critical patent/JPS5912348A/en
Publication of JPH0237984B2 publication Critical patent/JPH0237984B2/ja
Granted legal-status Critical Current

Links

Classifications

    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N27/00Investigating or analysing materials by the use of electric, electrochemical, or magnetic means
    • G01N27/02Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance
    • G01N27/04Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance
    • G01N27/14Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of an electrically-heated body in dependence upon change of temperature
    • G01N27/18Investigating or analysing materials by the use of electric, electrochemical, or magnetic means by investigating impedance by investigating resistance of an electrically-heated body in dependence upon change of temperature caused by changes in the thermal conductivity of a surrounding material to be tested
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
    • G01N33/20Metals
    • G01N33/202Constituents thereof
    • G01N33/2022Non-metallic constituents
    • G01N33/2025Gaseous constituents

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Immunology (AREA)
  • Pathology (AREA)
  • Analytical Chemistry (AREA)
  • Biochemistry (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Medicinal Chemistry (AREA)
  • Investigating And Analyzing Materials By Characteristic Methods (AREA)
  • Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)

Description

【発明の詳細な説明】 本発明は金属溶湯中の水素ガス濃度測定装置に
係り、特に溶融状態にある金属、なかでもアルミ
ニウム若しくはその合金溶湯中の溶存水素濃度を
直接測定し得る装置の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for measuring the concentration of hydrogen gas in molten metal, and more particularly to an improvement in an apparatus that can directly measure the concentration of dissolved hydrogen in molten metal, especially aluminum or its alloy. It is something.

従来より、アルミニウム若しくはアルミニウム
合金等の金属溶湯中に溶解乃至は溶存する水素ガ
スが、かかる溶湯の凝固の際に金属内部に気孔を
発生せしめ、この気孔が製品としての金属に種々
の弊害を及ぼすことが知られている。この気孔に
よる弊害は、従来にあつてはそれ程問題とされて
いなかつたのであるが、近年に至つて製品品質の
高級化が進み、例えば熱間加工工程でアルミニウ
ム板表面に生じた微小な「ふくれ」が、建材用パ
ネル材として製品化される際のアルマイト等の表
面処理工程において、ピツト状の欠陥を生じたり
して品質を損うなどの問題が指摘されるようにな
つてきてから、金属溶湯中の溶存水素を除去す
る、所謂脱水素操作がこれまで以上に重要な鋳造
作業の一工程となつてきている。
Conventionally, hydrogen gas dissolved or dissolved in molten metals such as aluminum or aluminum alloys generates pores inside the metal when the molten metal solidifies, and these pores have various harmful effects on the metal as a product. It is known. In the past, the harmful effects of these pores were not considered to be much of a problem, but as product quality has become higher in recent years, for example, minute "bulges" that occur on the surface of an aluminum plate during hot processing have become a problem. However, since it has been pointed out that problems such as the occurrence of pit-like defects and loss of quality in the surface treatment process of alumite, etc. when commercialized as panel materials for building materials, metal The so-called dehydrogenation operation, which removes dissolved hydrogen from molten metal, is becoming a more important step in casting operations than ever before.

ところで、かかる脱水素操作はその操作に時間
が長くかかり、また必要以上の脱水素操作は製品
のコストアツプを招くところから、通常はその操
作を行う前に予め金属溶湯中の溶存水素濃度を測
定し、その測定結果に基づいて必要最小限の脱水
素操作のみを施すのがよいとされている。
By the way, such a dehydrogenation operation takes a long time, and dehydrogenation operations longer than necessary will increase the cost of the product, so the concentration of dissolved hydrogen in the molten metal is usually measured beforehand. It is said that it is best to perform only the minimum necessary dehydrogenation operation based on the measurement results.

而して、金属溶湯中の溶存水素濃度を測定する
方法としては、上記と同様の理由、即ち、その測
定に要する時間が短くて済むというところから、
英国特許第684865号明細書、米国特許第2861450
号明細書等に示されるような装置を用いる、所謂
テレガス(Telegas)法を採用するのが望ましい
とされているのである。
Therefore, the method for measuring the dissolved hydrogen concentration in molten metal is based on the same reason as above, that is, the time required for the measurement is short.
British Patent No. 684865, US Patent No. 2861450
It is considered desirable to employ the so-called Telegas method, which uses a device such as that shown in the specification of the above patent.

かかるテレガス法に用いられる水素ガス濃度測
定装置、所謂テレガス装置は、金属溶湯中に浸し
た2つの孔を有する浸漬ヘツドの一方の孔から窒
素等の不活性ガスを溶湯内に送り込む一方、他方
の孔でその不活性ガスを回収し、その回収した不
活性ガスをポンプ、水素ガス濃度検出器、浸漬ヘ
ツドを介して再び溶湯内に送り込むという操作を
繰り返すことによつて、溶湯中の溶存水素濃度に
平衡した分圧の水素ガスを不活性ガス中に取り込
むようにした構成となつている。そして、このよ
うな不活性ガスの再循環によつて形成される水素
ガスを含む混合ガスの熱伝導度を、前記水素ガス
濃度検出器に設けた2つの検出セルのうちの一方
のセル(検出側)で熱線(フイラメント)型検出
素子(金属抵抗ワイヤ)の抵抗変化値として取り
出す一方、他方のセル(対照側)内に不活性ガス
(この場合窒素)と熱伝導度のほぼ等しい空気を
常に拡散せしめて、そのセル内の熱線型検出素子
の抵抗値を一定値に保つてこれを基準値として取
り出し、これら2つの検出素子の抵抗値の差、即
ち検出側の循環不活性ガス中に占める水素分圧の
大きさに基づく熱伝導度の変化分、ひいては水素
ガスの平衡分圧の大きさをブリツジ回路で非平衡
電流として取り出すようにしている。そして、そ
の電流値を、溶湯の温度に応じて予め作成された
非平衡電流と溶湯中の水素ガス濃度との関係を示
す検量線と呼ばれるグラフで照合して水素ガス濃
度を算出し、さらにこの値に各金属の種類によつ
て定まる補正定数を乗じて金属溶湯中の溶存水素
濃度を求めるようにしている。
The hydrogen gas concentration measuring device used in the telegas method, the so-called telegas device, has an immersion head that has two holes immersed in the molten metal. An inert gas such as nitrogen is sent into the molten metal through one hole, while the other is immersed in the molten metal. By repeating the process of recovering the inert gas through the holes and sending the recovered inert gas back into the molten metal via a pump, a hydrogen gas concentration detector, and an immersion head, the dissolved hydrogen concentration in the molten metal can be determined. The structure is such that hydrogen gas at a partial pressure balanced with the inert gas is introduced into the inert gas. The thermal conductivity of the mixed gas containing hydrogen gas formed by such recirculation of the inert gas is measured by one of the two detection cells (detection cell) provided in the hydrogen gas concentration detector. On the other hand, the resistance change value of the filament-type detection element (metallic resistance wire) is extracted in the other cell (on the control side), while air whose thermal conductivity is almost equal to that of the inert gas (nitrogen in this case) is always kept in the other cell (control side). The resistance value of the hot wire type detection element in the cell is maintained at a constant value, and this value is taken out as a reference value. The change in thermal conductivity based on the magnitude of the hydrogen partial pressure, and thus the magnitude of the equilibrium partial pressure of hydrogen gas, is extracted as a nonequilibrium current by the bridge circuit. Then, the hydrogen gas concentration is calculated by comparing the current value with a graph called a calibration curve that shows the relationship between the nonequilibrium current and the hydrogen gas concentration in the molten metal, which has been created in advance according to the temperature of the molten metal. The dissolved hydrogen concentration in the molten metal is determined by multiplying the value by a correction constant determined by the type of each metal.

かかる構成の従来のテレガス装置によれば、溶
湯状態の金属から直接溶存水素濃度(水素ガス濃
度)を測定できるため、その測定時間は、凝固し
た金属を試料として水素ガス濃度を測定する他の
方法に比べて短くて済むのであるが、作業能率の
面から見た場合には、いまだ十分に短縮されてい
るとは言い得なかつたのである。
According to the conventional telegas device with this configuration, the dissolved hydrogen concentration (hydrogen gas concentration) can be directly measured from the molten metal, so the measurement time is shorter than that of other methods that measure the hydrogen gas concentration using solidified metal as a sample. However, from the point of view of work efficiency, it could not be said that the time was sufficiently shortened.

即ち、前記従来のテレガス装置にあつては、水
素ガス濃度検出器の検出セルが黄銅等の金属ブロ
ツクに穿たれた孔をセル容器として直接利用した
構成とされているため、ブリツジ回路の2辺を構
成する熱線型検出素子と、これらの素子を収容す
る金属ブロツク、及びこの金属ブロツクの周囲の
雰囲気との間が熱的平衡状態となるまでにかなり
時間がかかり、それ故ブリツジ回路の電流計の指
示値が安定して、金属溶湯中の水素ガス濃度を算
出するまで比較的長時間を要したのである。
That is, in the conventional telegas device described above, the detection cell of the hydrogen gas concentration detector is configured to directly use a hole drilled in a metal block such as brass as a cell container. It takes a considerable amount of time for the hot-wire detection elements that make up the bridge circuit, the metal block that houses these elements, and the atmosphere surrounding this metal block to reach a state of thermal equilibrium, and therefore the bridge circuit ammeter It took a relatively long time until the indicated value became stable and the hydrogen gas concentration in the molten metal was calculated.

また、かかる装置にあつては、上記金属ブロツ
クが周囲の雰囲気の温度変化を受けた場合、その
金属ブロツクとその内部に収容されている熱線型
検出素子との間の熱平衡状態がくずれて、ブリツ
ジ回路の電流計の指示値が除々に変化してしまう
こととなるため、再度安定するようにかなりの時
間を必要とするだけでなく、その都度電流計の零
点校正を行なわなければならないという問題点を
も内在していたのである。
In addition, in such a device, when the metal block is subjected to a temperature change in the surrounding atmosphere, the thermal equilibrium state between the metal block and the hot wire type detection element housed therein is disrupted, and the bridge is damaged. The problem is that not only does it take a considerable amount of time to stabilize the circuit, but the ammeter must be zero-calibrated each time because the value indicated by the ammeter in the circuit changes gradually. It also contained within it.

本発明は、かかる事情を背景として為されたも
のであつて、その目的とするところは、測定時間
が短く、しかも周囲の雰囲気の温度変化によつて
その指示値が容易に変化しない、従つて零点校正
がそれ程必要でない金属溶湯中の水素ガス濃度測
定装置を提供することにある。
The present invention was developed against the background of the above circumstances, and its purpose is to shorten the measurement time and to prevent the indicated value from changing easily due to changes in the temperature of the surrounding atmosphere. An object of the present invention is to provide an apparatus for measuring hydrogen gas concentration in molten metal that does not require so much zero point calibration.

そして、その目的を達成する為に、本発明にあ
つては、金属溶湯中に浸漬され、循環せしめられ
る不活性ガスと金属溶湯との接触を行なう、かか
る不活性ガスの金属溶湯中への吹込み孔と該吹込
み孔を通じて吹き込まれた不活性ガスを金属溶湯
から分離するフイルタと該フイルタにて分離され
た不活性ガスを回収する回収孔とを備えた浸漬ヘ
ツドと;該浸漬ヘツドの吹込み孔と回収孔に接続
されて閉回路を構成する不活性ガス流路を有し、
ポンプ手段によつて、該流路を通じて不活性ガス
を繰り返し該浸漬ヘツドに循環、流通せしめる不
活性ガス循環機構と;前記不活性ガス流路上に設
けられ、気体の熱伝導度の変化によつて抵抗値が
変化する熱線型検出素子を用いて、該流路内を流
通せしめられる不活性ガス中に含まれる水素ガス
濃度に応じて変化する電気抵抗を検出する検出手
段とを;含む水素ガス濃度測定装置において、該
検出手段が、前記不活性ガス流路に接続された、
循環せしめられる水素含有不活性ガスに晒される
前記熱線型検出素子を収容した測定セルを有する
と共に、かかる測定セルの周囲に、それを取り巻
くように真空層を設けるようにしたのである。
In order to achieve this objective, the present invention involves blowing the inert gas into the molten metal, which brings the molten metal into contact with an inert gas that is immersed in the molten metal and circulated. an immersion head comprising an injection hole, a filter for separating an inert gas blown through the injection hole from the molten metal, and a recovery hole for recovering the inert gas separated by the filter; It has an inert gas flow path connected to the filling hole and the recovery hole to form a closed circuit,
an inert gas circulation mechanism that repeatedly circulates and flows an inert gas through the flow path to the immersion head by means of a pump means; a detection means that uses a hot wire type detection element whose resistance value changes to detect an electrical resistance that changes depending on the hydrogen gas concentration contained in the inert gas flowing through the flow path; In the measuring device, the detection means is connected to the inert gas flow path.
The measuring cell is provided with a measuring cell containing the hot wire type detection element that is exposed to the circulating hydrogen-containing inert gas, and a vacuum layer is provided around the measuring cell so as to surround it.

かかる構成の本発明によれば、水素含有不活性
ガスにさらされる熱線型検出素子を収容する測定
セルの周囲に真空層が設けられることにより、セ
ル自体の熱容量を効果的に小さく為し得るととも
に、該測定セルを、検出手段を取り巻く雰囲気か
ら熱的に遮断せしめ得るので、測定セルは周囲の
雰囲気の温度変化の影響を殆んど受けず、以て所
定の温度値に速やかに安定することとなり、これ
によつて零点校正がほとんど不要で、しかも測定
時間が大幅に短縮された水素ガス濃度測定装置が
得られることとなつたのである。そして、この測
定時間の短縮によつて作業能率がより向上し、以
て製品のコストダウンを図ることが可能となつた
のである。
According to the present invention having such a configuration, by providing a vacuum layer around the measurement cell housing the hot wire type detection element exposed to the hydrogen-containing inert gas, the heat capacity of the cell itself can be effectively reduced. , the measuring cell can be thermally isolated from the atmosphere surrounding the detection means, so that the measuring cell is almost unaffected by temperature changes in the surrounding atmosphere and quickly stabilizes at a predetermined temperature value. As a result, it has become possible to obtain a hydrogen gas concentration measuring device that requires almost no zero point calibration and that can significantly shorten the measurement time. This reduction in measurement time further improves work efficiency, making it possible to reduce product costs.

以下、本発明を更に具体的に明らかにするため
に、その二、三の実施例を図面に基づいて詳細に
説明する。
Hereinafter, in order to clarify the present invention more specifically, two or three embodiments thereof will be described in detail based on the drawings.

先ず、第1図は本発明に係る水素ガス濃度測定
装置の一実施例を示す系統図であるが、図におい
て、2はアルミニウム或はアルミニウム合金等の
金属溶湯4中に浸漬された2孔プローブ(浸漬ヘ
ツド)であつて、溶湯4中に深く延び出させられ
た第1の孔(吹込み孔)6と、その上方に設けら
れ、該第1の孔6から吹き出される窒素やアルゴ
ン等の不活性ガスの気泡を集めるようにしたスカ
ート8と、そのスカート8の内側上方に開口され
た第2の孔(回収孔)10と、該スカート8内を
仕切り、該第2の孔10に導かれる不活性ガス気
泡から溶湯を除く、該溶湯に対する濡れの少な
い、セラミツクスなどからなるフイルタ11とを
備えたものである。この2孔プローブ2の各孔6
及び10は、それぞれチユーブ12及び14を介
してダイヤフラムポンプ16に接続されており、
そのダイヤフラムポンプ16及びチユーブ12,
14等によつて構成される不活性ガス循環機構と
前記溶湯4とともに、不活性ガスの閉流路を形成
している。
First, FIG. 1 is a system diagram showing an embodiment of the hydrogen gas concentration measuring device according to the present invention. In the figure, 2 is a two-hole probe immersed in a molten metal 4 of aluminum or aluminum alloy. (immersion head), which has a first hole (blow hole) 6 that extends deeply into the molten metal 4, and nitrogen, argon, etc. that are provided above the first hole and are blown out from the first hole 6. A skirt 8 configured to collect inert gas bubbles, a second hole (collection hole) 10 opened upward inside the skirt 8; It is equipped with a filter 11 made of ceramics or the like that is less wetted by the molten metal and removes the molten metal from the guided inert gas bubbles. Each hole 6 of this two-hole probe 2
and 10 are connected to a diaphragm pump 16 via tubes 12 and 14, respectively,
the diaphragm pump 16 and tube 12,
14 and the like and the molten metal 4 form a closed flow path for inert gas.

すなわち、上記チユーブ12及び14上には逆
止弁18及び20がそれぞれ設けられており、こ
の逆止弁18及び20によつて、不活性ガスが上
記流路内を2孔プローブ2の第1の孔6から溶湯
4内に吹き出す方向に流通せしめられるようにな
つているのであり、モータ22によるダイヤフラ
ムポンプ16の作動によつて、不活性ガスが前記
閉流路内を繰り返し循環されるのである。
That is, check valves 18 and 20 are provided on the tubes 12 and 14, respectively, and the check valves 18 and 20 allow the inert gas to pass through the flow path to the first side of the two-hole probe 2. The inert gas is made to flow in the direction of blowing out into the molten metal 4 from the hole 6, and the inert gas is repeatedly circulated within the closed flow path by the operation of the diaphragm pump 16 by the motor 22. .

そして、この不活性ガスの循環の際、プローブ
2の第1の孔6から溶湯4中に吹き出された不活
性ガスは、溶湯4中を気泡となつてスカート8ま
で達するのであるが、この間に溶湯4中に溶解さ
れている水素が上記気泡中に拡散するのであり、
そして不活性ガスが前記閉流路内を繰り返し循環
せしめられることにより、不活性ガス気泡中に拡
散する水素の分圧が徐々に上昇して、ついには溶
湯4中に溶解されている水素濃度と平衡する分圧
にまで高められるのである。なお、水素は上記平
衡分圧以上には不活性ガス中に拡散することはな
いのである。
During this inert gas circulation, the inert gas blown into the molten metal 4 from the first hole 6 of the probe 2 becomes bubbles in the molten metal 4 and reaches the skirt 8. Hydrogen dissolved in the molten metal 4 diffuses into the bubbles,
As the inert gas is repeatedly circulated within the closed flow path, the partial pressure of hydrogen diffusing into the inert gas bubbles gradually increases, and finally the concentration of hydrogen dissolved in the molten metal 4 increases. The partial pressure is increased to equilibrium. Note that hydrogen does not diffuse into the inert gas above the above equilibrium partial pressure.

かかる平衡分圧に差した水素ガスを含む不活性
ガス、所謂水素含有不活性ガスは、そこに含有さ
れる水素ガスの分圧に応じて熱伝導度が高くなつ
ているところから、この熱伝導度の大きさをチユ
ーブ14上に設けられた水素ガス濃度検出器24
で検出するようにしているのである。
Inert gas containing hydrogen gas that is below the equilibrium partial pressure, so-called hydrogen-containing inert gas, has thermal conductivity that increases according to the partial pressure of hydrogen gas contained therein. The hydrogen gas concentration detector 24 installed on the tube 14
This is how it is detected.

この水素ガス濃度検出器24は、例えば第2図
に示されるように、アルミニウム或は黄銅等の検
出器ブロツク26に、水素含有不活性ガスと空気
のそれぞれの熱伝導度を測定するための2つの検
出部27,27が形成されたペア構造とされてお
り、各々の検出部27は検出器ブロツク26に形
成されたシリンダ28内に更に測定セル30が収
容された2重構造とされている。
For example, as shown in FIG. 2, this hydrogen gas concentration detector 24 includes a detector block 26 made of aluminum or brass, and a detector block 26 for measuring the respective thermal conductivities of hydrogen-containing inert gas and air. It has a pair structure in which two detection parts 27, 27 are formed, and each detection part 27 has a double structure in which a measurement cell 30 is further housed in a cylinder 28 formed in the detector block 26. .

すなわち、第2図において、32は断熱性材料
からなる円筒形状の第1シール部材であつて、そ
の内側空間下部に、ステンレス等の金属材料から
なる有底円筒形状のセル容器34の開口部が嵌
入・接着せしめられるとともに、その内側空間上
部にやはり断熱性材料からなる第2シール部材3
6が嵌め込まれており、かかる第1シール部材3
2が各シリンダ28の開口部に気密に嵌入され
て、シリンダ28内においてセル容器34の内外
に、互に気密な空間であるガス拡散室38及び真
空室40を形成している。
That is, in FIG. 2, 32 is a cylindrical first sealing member made of a heat insulating material, and the opening of a bottomed cylindrical cell container 34 made of a metal material such as stainless steel is located in the lower part of the inner space. A second sealing member 3 made of a heat insulating material is also fitted and bonded, and is also made of a heat insulating material at the upper part of the inner space.
6 is fitted into the first seal member 3.
2 is hermetically fitted into the opening of each cylinder 28 to form a gas diffusion chamber 38 and a vacuum chamber 40, which are mutually airtight spaces, inside and outside the cell container 34 within the cylinder 28.

一方の検出部27のガス拡散室38は、第1シ
ール部材32に形成された通孔42,42a,4
2bを介して、水素含有不活性ガスの流路である
チユーブ14,14a,14bに接続されてお
り、水素含有不活性ガスが一方のチユーブ14a
から通孔部分42aを通つて該ガス拡散室38内
上部を通過し、他方の通孔部分42bを通つてチ
ユーブ14bに流出するようにされている。ま
た、他方の検出部27のガス拡散室38はチユー
ブ44,44a,44bによつて外気に接続され
ており、測定セル30内には不活性ガスと熱伝導
度のほぼ等しい空気が充填されるようになつてい
る。
The gas diffusion chamber 38 of one of the detection parts 27 includes through holes 42, 42a, 4 formed in the first sealing member 32.
2b to tubes 14, 14a, and 14b, which are flow paths for hydrogen-containing inert gas, and the hydrogen-containing inert gas flows through one tube 14a.
The gas passes through the through-hole portion 42a, passes through the upper part of the gas diffusion chamber 38, and flows out into the tube 14b through the other through-hole portion 42b. Further, the gas diffusion chamber 38 of the other detection section 27 is connected to the outside air through tubes 44, 44a, and 44b, and the measurement cell 30 is filled with air having approximately the same thermal conductivity as the inert gas. It's becoming like that.

そして、これらの拡散室38内、即ち測定セル
30内に、それぞれ拡散される気体(ガス)の熱
伝導度の変化によつて温度、即ち抵抗値が変化す
る白金等のワイヤからなる熱線型検出素子(電気
抵抗ワイヤ)46が設けられ、水素含有不活性ガ
ス若しくは空気の熱伝導度を抵抗値として検出す
るようにされているのである。なお、この時、水
素ガスの分圧が大きい程、水素ガス含有不活性ガ
スの熱伝導度が高く、熱線型抵抗素子46はより
冷却されてその抵抗値が低くなるのであり、後述
の非平衡電流がより多く流されるのである。
Inside these diffusion chambers 38, that is, inside the measurement cells 30, there is a hot wire type detection device made of a wire made of platinum or the like whose temperature, or resistance value, changes depending on the change in thermal conductivity of the gas being diffused. An element (electrical resistance wire) 46 is provided to detect the thermal conductivity of the hydrogen-containing inert gas or air as a resistance value. At this time, the higher the partial pressure of hydrogen gas, the higher the thermal conductivity of the hydrogen gas-containing inert gas, and the hot wire type resistance element 46 is cooled more and its resistance value is lowered. More current will flow through it.

また、本実施例にあつては、上記熱線型検出素
子46は、第2シール部材36からセル容器34
内に向つて延設(垂下)された、アルミナ或はセ
ラミツクス等の非導電性材料からなる中空パイプ
(支持体)48の下端部で曲げられ、その一方が
該パイプ48内を通つて、またその他方が該パイ
プ48の外側面を上方に向つて巻き付けられて、
共に第2シール部材36内を貫通して設けられた
白金線ステム46a,46bに接続され、これら
の白金線ステム46a,46bが更に後述のホイ
ートストンブリツジ回路50からの導線51a,
51b並びに51c,51dにそれぞれ接続され
ているのである。
Further, in this embodiment, the hot wire type detection element 46 is connected to the cell container 34 from the second sealing member 36.
A hollow pipe (supporting body) 48 made of a non-conductive material such as alumina or ceramics is bent at the lower end, extending (hanging) inward, and one side passes through the inside of the pipe 48, and the other end is bent. The other end is wrapped upwardly around the outer surface of the pipe 48,
Both are connected to platinum wire stems 46a and 46b provided through the second seal member 36, and these platinum wire stems 46a and 46b are further connected to conductors 51a and 51a from a Wheatstone bridge circuit 50, which will be described later.
51b, 51c, and 51d, respectively.

このように、電気抵抗ワイヤ46を支持体に巻
き付けて保持すれば、振動によつて該電気抵抗ワ
イヤが中間部で互に接触したり、セル壁に衝突し
たりして破損する等の問題を惹起する恐れがなく
なり、寿命が長く且つ検出値誤差の少ない測定セ
ルが得られる利点がある。
If the electrical resistance wires 46 are held by being wound around the support in this way, problems such as the electrical resistance wires coming into contact with each other in the middle or colliding with the cell wall due to vibration and being damaged can be avoided. This has the advantage that a measurement cell with a long service life and little error in detected values can be obtained.

一方、各検出部27,27の真空室40は、検
出器ブロツク26内で互に連通されており、予め
それら真空室40に連通されるパイプ52に接続
される図示しない真空ポンプによつて真空状態と
された後、図示しない真空締付け具やろう付け等
の公知の手段によつて密封されている。
On the other hand, the vacuum chambers 40 of each of the detection units 27, 27 are communicated with each other within the detector block 26, and a vacuum pump (not shown) connected to a pipe 52 communicating with the vacuum chambers 40 is used to generate a vacuum. After this state, it is sealed by known means such as vacuum fasteners or brazing (not shown).

かかる構造の水素ガス濃度検出器24で各々抵
抗値に変換された水素含有不活性ガス及び空気の
熱伝導度は、第1図に示されるように、ホイート
ストンブリツジ回路50で比較されて、それらの
熱伝導度(抵抗値)の差に応じた非平衡電流とし
て取り出され、この非平衡電流がホイートストン
ブリツジ回路50に接続された演算処理回路(コ
ンピユータ)54に送られて、そこで所定の関係
式によつて演算・表示されることによつて、測定
した金属溶湯中の水素ガス濃度(溶存水素濃度)
が即座に把握されるようになつている。なお、5
6は溶湯4中に浸された熱電対であつて、上記演
算処理回路54に溶湯4の温度データを提供する
ものであり、また58は前記ホイートストンブリ
ツジ回路50及び演算処理回路54に電流を供給
する定電圧(定電流)電源回路である。
The thermal conductivities of the hydrogen-containing inert gas and air, each converted into a resistance value by the hydrogen gas concentration detector 24 having such a structure, are compared in a Wheatstone bridge circuit 50 as shown in FIG. This non-balanced current is extracted as an unbalanced current corresponding to the difference in thermal conductivity (resistance value) of The hydrogen gas concentration (dissolved hydrogen concentration) in the measured molten metal is calculated and displayed using the formula.
can now be grasped instantly. In addition, 5
6 is a thermocouple immersed in the molten metal 4, which provides temperature data of the molten metal 4 to the arithmetic processing circuit 54; and 58, which supplies current to the Wheatstone bridge circuit 50 and the arithmetic processing circuit 54. This is a constant voltage (constant current) power supply circuit.

また、第1図において、60は不活性ガスボン
ベであつて、該ボンベから所定の不活性ガス、例
えば窒素ガスなどがチユーブ62を介して、水素
ガス濃度検出器24と逆止弁20との間のチユー
ブ14部分に導入されるようになつている。な
お、チユーブ62上に設けられたストツパバルブ
64によつて、該ボンベ60からの不活性ガスの
供給が制御されるようになつているのである。
Further, in FIG. 1, reference numeral 60 denotes an inert gas cylinder, from which a predetermined inert gas such as nitrogen gas is supplied between the hydrogen gas concentration detector 24 and the check valve 20 via a tube 62. It is designed to be introduced into the tube 14 portion of the tube. Note that the supply of inert gas from the cylinder 60 is controlled by a stopper valve 64 provided on the tube 62.

かかる構成の水素ガス濃度測定装置によつて金
属溶湯4中の水素濃度を測定する場合には、定電
圧電源回路58を作動した状態でストツパバルブ
64を開き、ボンベ60内の不活性ガスを前記閉
流路内に充填せしめた後、2孔プローブ2を静か
に溶湯4中に浸漬せしめ、その後ストツパバルブ
64を閉じて流路内への不活性ガスの供給を停止
する。この時、熱電対56も溶湯4中に浸漬せし
め、演算処理回路54の指示値が0であることを
確認する。指示値が0であることを確認した後、
モータ22によつてダイヤフラムポンプ16を作
動せしめ、不活性ガスを前記閉流路内で繰り返し
循環・流通せしめる。そして、演算処理回路54
の指示値が安定したことを確かめ、その最終安定
値を測定値として読み取るのである。
When measuring the hydrogen concentration in the molten metal 4 with the hydrogen gas concentration measuring device having such a configuration, the stopper valve 64 is opened while the constant voltage power supply circuit 58 is operated, and the inert gas in the cylinder 60 is discharged from the above-mentioned closed state. After filling the flow path, the two-hole probe 2 is gently immersed in the molten metal 4, and then the stopper valve 64 is closed to stop the supply of inert gas into the flow path. At this time, the thermocouple 56 is also immersed in the molten metal 4, and it is confirmed that the indicated value of the arithmetic processing circuit 54 is 0. After confirming that the indicated value is 0,
The diaphragm pump 16 is operated by the motor 22, and the inert gas is repeatedly circulated and distributed within the closed flow path. Then, the arithmetic processing circuit 54
After confirming that the indicated value has stabilized, the final stable value is read as the measured value.

以上説明したような本実施例によれば、測定セ
ル30の周囲に設けた真空室40によつて、セル
容器34が外気から断熱されるとともに、セル容
器34自体の熱容量が効果的に小さくされている
ので、測定値が早く安定することになり、以て測
定時間が短縮されることとなつたのである。
According to this embodiment as described above, the vacuum chamber 40 provided around the measurement cell 30 insulates the cell container 34 from the outside air and effectively reduces the heat capacity of the cell container 34 itself. As a result, the measured values stabilized quickly, and the measurement time was thereby shortened.

因みに、本発明者らが実験した結果によれば、
従来のテレガス装置による非平衡出力:(mV)
の経時的な変化の状態は、第3図に1点鎖線で示
され、一方本実施例の水素ガス濃度測定装置によ
る非平衡出力:(mV)の経時的変化状態は、
第3図に実線で示されるものであつた。第3図の
実験結果から明らかなように、従来のテレガス装
置にあつては、測定開始後(検出器並びにその付
属回路の電源スイツチを投入後)24分経過した時
点でも、その指示値はいまだ安定しておらず、一
方本実施例装置にあつては、測定開始後約10分で
指示値が安定(熱的平衡状態)となり、これによ
つて、本実施例に係る装置による金属溶湯中の水
素ガス濃度の測定時間が従来装置のそれに比べて
極めて短縮されたことがわかる。
Incidentally, according to the results of experiments conducted by the present inventors,
Unbalanced output by conventional telegas equipment: (mV)
The state of change over time of is shown in FIG.
This was shown by the solid line in FIG. As is clear from the experimental results shown in Figure 3, in the case of conventional telegas equipment, even after 24 minutes have passed after the start of measurement (after turning on the power switch for the detector and its attached circuits), the indicated value still remains. On the other hand, in the case of the device of this example, the indicated value becomes stable (thermal equilibrium state) approximately 10 minutes after the start of measurement, and as a result, the temperature in the molten metal by the device of this example becomes stable. It can be seen that the measurement time for the hydrogen gas concentration was significantly shortened compared to that of the conventional device.

なお、上記非平衡出力:は、熱の輻射・対流
が無視できるものとして次式によつて表わされる
値である。
Note that the above non-equilibrium output is a value expressed by the following equation assuming that heat radiation and convection can be ignored.

=1/2I・Rf・a(tf−tc)/1+atf・δ・γ
/1+γ ここにおいて、Iはホイートストンブリツジ回
路に供給される直流電流、Rfは水素含有不活性
ガス流入側の電気抵抗ワイヤの抵抗値、αは同じ
く電気抵抗ワイヤの温度係数、tfは同じく電気抵
抗ワイヤの温度、tcは測定セルの内壁温度、δは
測定セル内の平均温度における不活性ガスのみの
熱伝導度λmに対する(水素ガス流入による)熱
伝導度の変化量Δλの比、γはRfに対する空気流
入側の電気抵抗ワイヤの抵抗値Rの比、Rrは記
録計の入力インピーダンスである。ただし、 2Rr≫Rf+R の関係があるものとする。
=1/2I・Rf・a(tf−tc)/1+atf・δ・γ
/1+γ Here, I is the DC current supplied to the Wheatstone bridge circuit, R f is the resistance value of the electrical resistance wire on the hydrogen-containing inert gas inflow side, α is the temperature coefficient of the electrical resistance wire, and tf is the electrical resistance wire. The temperature of the resistance wire, tc is the inner wall temperature of the measurement cell, δ is the ratio of the amount of change in thermal conductivity Δλ (due to hydrogen gas inflow) to the thermal conductivity λm of only inert gas at the average temperature in the measurement cell, and γ is Rr, the ratio of the resistance value R of the electrical resistance wire on the air inflow side to Rf, is the input impedance of the recorder. However, it is assumed that there is a relationship of 2Rr≫R f +R.

また、本実施例では水素ガス濃度検出器24を
第2図に示すような構成としたが、これに限られ
るものではなく、第4図及び第5図に示されるよ
うな構成のものであつても何等差支えない。
Further, in this embodiment, the hydrogen gas concentration detector 24 has a configuration as shown in FIG. 2, but is not limited to this, and may have a configuration as shown in FIGS. 4 and 5. It doesn't make any difference.

すなわち、第4図に示される水素ガス濃度検出
器66の測定セル67は、第1シール部材68に
形成されたシリンダ28の内外を連通する通孔7
0に、チユーブ14a,14bとチユーブ72
a,72bが内外からそれぞれ気密に挿入・接着
されるとともに、チユーブ72a,72bの他端
がセル容器34の下端部においてガス拡散室38
にそれぞれ接続された構成とされており、該拡散
室38の下部から上方に向つて水素ガスが拡散せ
しめられるようになつているのである。なお、他
の部分の構成は前記実施例と同じであるため、同
一の符号を符して詳細な説明は省略する。
That is, the measurement cell 67 of the hydrogen gas concentration detector 66 shown in FIG.
0, tubes 14a, 14b and tube 72
a, 72b are hermetically inserted and bonded from the inside and outside, respectively, and the other ends of the tubes 72a, 72b are connected to the gas diffusion chamber 38 at the lower end of the cell container 34.
The diffusion chamber 38 is configured such that hydrogen gas is diffused upward from the lower part of the diffusion chamber 38. Note that since the configuration of other parts is the same as in the previous embodiment, the same reference numerals are used and detailed explanations are omitted.

また、第5図に示されるものにあつては、各測
定セル74は金属管76を外筒とするシリンダ2
8内に収容されており、また各金属管76は溶接
によつてパイプ52に直接取り付けられている。
そして各チユーブ14a,14bは、金属管76
の側壁に設けられた穴及び第1シール部材78に
形成された通孔80を介してガス拡散室38の上
部に接続されているのである。なお、中空パイプ
48はその上端部が栓部材で塞がれて、その内部
空間が外部雰囲気に対して気密に保たれている。
In addition, in the case shown in FIG. 5, each measurement cell 74 has a cylinder 2 whose outer cylinder is a metal tube 76.
8 and each metal tube 76 is directly attached to the pipe 52 by welding.
Each tube 14a, 14b is a metal tube 76.
It is connected to the upper part of the gas diffusion chamber 38 through a hole provided in the side wall of the gas diffusion chamber 38 and a through hole 80 formed in the first seal member 78 . Note that the upper end of the hollow pipe 48 is closed with a plug member to keep the internal space airtight from the external atmosphere.

この第5図に示されるような構成の水素ガス濃
度検出器82は、金属管76を直接シリンダ28
として使用できるのでコンパクトに構成すること
が可能であり、恒温槽内に配置する場合により効
果的である。
The hydrogen gas concentration detector 82 configured as shown in FIG.
It can be used as a compact structure, and is more effective when placed in a constant temperature bath.

なお、前例においては、本発明を何れも拡散式
の水素ガス濃度検出器に適用した場合についての
み説明したが、半拡散式或は流通式の水素ガス濃
度検出器についても本発明の適用が可能である。
In the previous example, the present invention was explained only when applied to a diffusion type hydrogen gas concentration detector, but the present invention can also be applied to a semi-diffusion type or flow type hydrogen gas concentration detector. It is.

また、前記実施例においては、比較の基準とさ
れる測定セル側は全て大気に開放されていたが、
もちろんこれに限られるものではなく、大気の代
りに水素ガス濃度測定用の不活性ガスと同じ不活
性ガスが水素濃度測定用の閉回路流路とは別の閉
回路流路によつて測定セル内に供給されるように
なつていてもよいのである。要するに基準用の測
定セル側には水素ガス濃度測定用の不活性ガスと
同じ熱伝導度を有する気体が供給されればよく、
これによつて基準となる熱伝導度が検出されるよ
うになつていればよいのである。
In addition, in the above example, the measurement cell side, which is the standard for comparison, was all open to the atmosphere.
Of course, this is not limited to this, and instead of the atmosphere, the same inert gas as the inert gas for hydrogen gas concentration measurement is passed through the measurement cell through a closed circuit flow path different from the closed circuit flow path for hydrogen concentration measurement. It may also be supplied internally. In short, it is sufficient that a gas having the same thermal conductivity as the inert gas for hydrogen gas concentration measurement is supplied to the reference measurement cell.
It is only necessary that the thermal conductivity, which serves as a reference, be detected in this way.

その他、本発明に係る水素ガス濃度測定装置に
あつては、特許請求の範囲に記載した本発明の趣
旨を逸脱しない範囲内において、種々の変形・修
正を施した態様で実施することが可能である。例
えば、演算処理回路54を使用せずに、従来通り
測定した不平衡電流を検量線で照合して金属溶湯
中の水素ガス濃度を算出するようにしてもよいの
であり、また、ダイヤフラムポンプ16を駆動す
るのに、モータ22の代わりに不活性ガスを弁機
構で制御して駆動するようにしてもよいのであ
る。
In addition, the hydrogen gas concentration measuring device according to the present invention can be implemented with various modifications and modifications without departing from the spirit of the present invention as set forth in the claims. be. For example, without using the arithmetic processing circuit 54, the hydrogen gas concentration in the molten metal may be calculated by comparing the conventionally measured unbalanced current with a calibration curve. Instead of the motor 22, inert gas may be controlled and driven using a valve mechanism.

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

第1図は本発明に係る水素ガス濃度測定装置の
一実施例を示す系統図であり、第2図はその装置
に使用される水素ガス濃度検出器の一例を示す要
部断面図である。第3図は第2図に示される水素
ガス濃度検出器並びに従来のテレガス装置を用い
て金属溶湯中の水素ガスを測定した場合の実験結
果を非平衡出力:の経時的な変化状態として示
すものである。第4図並びに第5図は、それぞれ
本発明装置に使用される水素ガス濃度検出器の別
の例を示す要部断面図である。 2:2孔プローブ、4:金属溶湯、16:ダイ
ヤフラムポンプ、22:モータ、24,66,8
2:水素ガス濃度検出器、26:検出器ブロツ
ク、27:検出器、28:シリンダ、30,6
7,74:測定セル、32,68,78:第1シ
ール部材、34:セル容器、36:第2シール部
材、38:ガス拡散室、40:真空室、46:熱
線型検出素子、48:中空パイプ、50:ホイー
トストンブリツジ回路、54:演算処理回路、5
6:熱電対、76:金属管。
FIG. 1 is a system diagram showing an embodiment of a hydrogen gas concentration measuring device according to the present invention, and FIG. 2 is a sectional view of essential parts showing an example of a hydrogen gas concentration detector used in the device. Figure 3 shows the experimental results of measuring hydrogen gas in molten metal using the hydrogen gas concentration detector shown in Figure 2 and a conventional telegas device as a change over time in the nonequilibrium output. It is. FIGS. 4 and 5 are sectional views of main parts showing other examples of hydrogen gas concentration detectors used in the apparatus of the present invention, respectively. 2: 2-hole probe, 4: Molten metal, 16: Diaphragm pump, 22: Motor, 24, 66, 8
2: Hydrogen gas concentration detector, 26: Detector block, 27: Detector, 28: Cylinder, 30, 6
7, 74: measurement cell, 32, 68, 78: first seal member, 34: cell container, 36: second seal member, 38: gas diffusion chamber, 40: vacuum chamber, 46: hot wire type detection element, 48: Hollow pipe, 50: Wheatstone bridge circuit, 54: Arithmetic processing circuit, 5
6: Thermocouple, 76: Metal tube.

Claims (1)

【特許請求の範囲】 1 金属溶湯4中に浸漬され、循環せしめられる
不活性ガスと金属溶湯との接触を行なう、かかる
不活性ガスの金属溶湯中への吹込み孔6と該吹込
み孔を通じて吹き込まれた不活性ガスを金属溶湯
から分離するフイルタ11と該フイルタにて分離
された不活性ガスを回収する回収孔10とを備え
た浸漬ヘツド2と;該浸漬ヘツドの吹込み孔と回
収孔に接続されて閉回路を構成する不活性ガス流
路12,14を有し、ポンプ手段16によつて、
該流路を通じて不活性ガスを繰り返し該浸漬ヘツ
ドに循環、流通せしめる不活性ガス循環機構と;
前記不活性ガス流路上に設けられ、気体の熱伝導
度の変化によつて抵抗値が変化する熱線型検出素
子46を用いて、該流路内を流通せしめられる不
活性ガス中に含まれる水素ガス濃度に応じて変化
する電気抵抗を検出する検出手段24とを;含む
水素ガス濃度測定装置において、 該検出手段24が、前記不活性ガス流路に接続
された、循環せしめられる水素含有不活性ガスに
晒される前記熱線型検出素子46を収容した測定
セル30,67,74を有すると共に、かかる測
定セルの周囲に、それを取り巻くように真空層4
0が設けられていることを特徴とする金属溶湯中
の水素ガス濃度測定装置。 2 前記熱線型検出素子46が、前記測定セル内
に挿入された支持体48に巻き付けられて保持さ
れている特許請求の範囲第1項記載の装置。 3 前記測定セル30,67が所定のブロツク2
6に設けられた孔28に装着され、そして該孔に
接続された真空手段の真空作用によつて、前記真
空層40が、該孔の内壁面と該測定セル外側面と
の間に形成される特許請求の範囲第1項または第
2項記載の装置。 4 前記測定セル74が二重筒構造の内筒部材を
構成し、該内筒部材とその外側に位置する外筒部
材76との間の空間が前記真空層とされた特許請
求の範囲第1項または第2項記載の装置。
[Scope of Claims] 1. An inert gas immersed in the molten metal 4 and brought into contact with the circulated inert gas and the molten metal, through a blowing hole 6 for the inert gas into the molten metal and the blowing hole. An immersion head 2 equipped with a filter 11 for separating the blown inert gas from the molten metal and a recovery hole 10 for recovering the inert gas separated by the filter; an injection hole and a recovery hole of the immersion head; It has inert gas passages 12 and 14 connected to it to constitute a closed circuit, and by means of a pump means 16,
an inert gas circulation mechanism that repeatedly circulates and flows inert gas to the immersion head through the flow path;
Hydrogen contained in the inert gas flowing through the inert gas flow path is detected using a hot wire type detection element 46 which is provided on the inert gas flow path and whose resistance value changes depending on the change in thermal conductivity of the gas. A hydrogen gas concentration measuring device including a detection means 24 for detecting electrical resistance that changes depending on the gas concentration, wherein the detection means 24 is a hydrogen-containing inert gas that is connected to the inert gas flow path and is circulated. It has measurement cells 30, 67, 74 that house the hot wire type detection element 46 exposed to gas, and a vacuum layer 4 surrounding the measurement cell.
1. An apparatus for measuring hydrogen gas concentration in molten metal, characterized in that a 0 is provided. 2. The device according to claim 1, wherein the hot wire type detection element 46 is held by being wound around a support 48 inserted into the measurement cell. 3 The measurement cells 30, 67 are in a predetermined block 2
By the vacuum action of vacuum means fitted and connected to the hole 28 provided in the hole 6, said vacuum layer 40 is formed between the inner wall surface of said hole and the outer surface of said measuring cell. An apparatus according to claim 1 or 2. 4. Claim 1, wherein the measurement cell 74 constitutes an inner cylinder member with a double cylinder structure, and the space between the inner cylinder member and the outer cylinder member 76 located outside thereof is the vacuum layer. 2. The device according to item 2 or item 2.
JP57122386A 1982-07-14 1982-07-14 Measuring device for concentration of hydrogen gas in molten metal Granted JPS5912348A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
JP57122386A JPS5912348A (en) 1982-07-14 1982-07-14 Measuring device for concentration of hydrogen gas in molten metal
GB08300562A GB2123957B (en) 1982-07-14 1983-01-10 Apparatus for measuring the content of hydrogen dissolved in a molten metal
DE3303122A DE3303122C2 (en) 1982-07-14 1983-01-31 Device for measuring the content of hydrogen dissolved in molten metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57122386A JPS5912348A (en) 1982-07-14 1982-07-14 Measuring device for concentration of hydrogen gas in molten metal

Publications (2)

Publication Number Publication Date
JPS5912348A JPS5912348A (en) 1984-01-23
JPH0237984B2 true JPH0237984B2 (en) 1990-08-28

Family

ID=14834513

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57122386A Granted JPS5912348A (en) 1982-07-14 1982-07-14 Measuring device for concentration of hydrogen gas in molten metal

Country Status (3)

Country Link
JP (1) JPS5912348A (en)
DE (1) DE3303122C2 (en)
GB (1) GB2123957B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61250556A (en) * 1985-04-30 1986-11-07 Nippon Kokan Kk <Nkk> Probe for quantitative analysis of C, S, N, H in molten steel
JPS61292055A (en) * 1985-06-19 1986-12-22 Nippon Kokan Kk <Nkk> Quick analysis of molten steel
JPS6256849A (en) * 1985-09-06 1987-03-12 Snow Brand Milk Prod Co Ltd Sensor used for electric heating method
JPH0613491Y2 (en) * 1985-10-11 1994-04-06 住友軽金属工業株式会社 Probe for measuring hydrogen concentration in molten metal
BE1000413A3 (en) * 1987-03-18 1988-11-22 Electro Nite Liquid metal gas content measuring probe - has lance and probe for bubbling gas through liquid metal and collecting gas bubbled through for detection
DE3868192D1 (en) * 1987-03-18 1992-03-12 Electro Nite DEVICE AND METHOD FOR MEASURING THE GAS CONTENT OF A LIQUID METAL AND PROBE THEREFOR.
US4829810A (en) * 1988-01-04 1989-05-16 Aluminum Company Of America Filament drive circuit
JPH0271151A (en) * 1988-09-07 1990-03-09 Sumitomo Light Metal Ind Ltd Concentration measuring device of hydrogen in molten metal
ZA898697B (en) * 1988-11-17 1990-09-26 Alcan Int Ltd Method and apparatus for determination of gas concentration in molten metal and metal matrix composites

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB821821A (en) * 1954-08-10 1959-10-14 British Aluminium Co Ltd Improvements in the determination of the gas content of liquid metals

Also Published As

Publication number Publication date
GB8300562D0 (en) 1983-02-09
JPS5912348A (en) 1984-01-23
DE3303122C2 (en) 1986-08-07
GB2123957A (en) 1984-02-08
GB2123957B (en) 1985-12-11
DE3303122A1 (en) 1984-01-19

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