JPH0149891B2 - - Google Patents
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- Publication number
- JPH0149891B2 JPH0149891B2 JP3077683A JP3077683A JPH0149891B2 JP H0149891 B2 JPH0149891 B2 JP H0149891B2 JP 3077683 A JP3077683 A JP 3077683A JP 3077683 A JP3077683 A JP 3077683A JP H0149891 B2 JPH0149891 B2 JP H0149891B2
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- Prior art keywords
- molten metal
- particle
- counter electrode
- pipe
- probe
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- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N21/00—Investigating or analysing materials by the use of optical means, i.e. using sub-millimetre waves, infrared, visible or ultraviolet light
- G01N21/62—Systems in which the material investigated is excited whereby it emits light or causes a change in wavelength of the incident light
- G01N21/71—Systems in which the material investigated is excited whereby it emits light or causes a change in wavelength of the incident light thermally excited
- G01N21/73—Systems in which the material investigated is excited whereby it emits light or causes a change in wavelength of the incident light thermally excited using plasma burners or torches
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- Health & Medical Sciences (AREA)
- Physics & Mathematics (AREA)
- Chemical & Material Sciences (AREA)
- Plasma & Fusion (AREA)
- Nuclear Medicine, Radiotherapy & Molecular Imaging (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
Description
【発明の詳細な説明】
本発明は、溶融金属表面と対電極間に高電圧を
かけて、スパークなどの電気的放電を行わせ、溶
融金属中の成分組成を代表する超微粒子を蒸発さ
せ、これを離れた場所に設定してあるプラズマ発
光分光分析装置に不活性ガス流で搬送し、溶融金
属中の各種成分含有率を、オンラインリアルタイ
ムで分析することを目的とする溶融金属の直接発
光分光分析装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention applies a high voltage between the molten metal surface and a counter electrode to cause electrical discharge such as a spark to evaporate ultrafine particles representative of the component composition in the molten metal. Direct emission spectroscopy of molten metal is carried out using an inert gas flow to analyze the content of various components in the molten metal in real time online by transporting the molten metal to a plasma emission spectrometer set up at a remote location. This relates to an analytical device.
金属製造業における製造工程管理には、サンプ
リングして固化させたブロツク試料を対象とする
スパーク発光分光分析が多用されている。しか
し、近年とくに鉄鋼業に見られるように、より迅
速な製造工程管理あるいは多段精錬製鋼法などの
新製造プロセスの操業管理のために、溶銑や溶鋼
のような溶融金属を直接対象とするオンラインリ
アルタイムの分析手法の開発が強く要請されてい
る。 Spark emission spectroscopic analysis of sampled and solidified block samples is often used for manufacturing process control in the metal manufacturing industry. However, in recent years, especially in the steel industry, online real-time technology that directly targets molten metals such as hot pig iron and molten steel has become available for faster manufacturing process control or operational management of new manufacturing processes such as multi-stage refining steelmaking. There is a strong need to develop analytical methods for this.
これまで、溶融金属をArガスを用いた特殊な
噴霧器によつて微粉化して、発光分光分析する方
法(BISRA,Annual Report:78(1966),65,
78(1967),35(1968))など各種の手法により研究
開発が試みられてきた。しかし、これらの方法は
これまで実際に製造現場で実用されたことはな
く、いずれも実験室規模で試みられたに過ぎな
い。 Until now, the method of pulverizing molten metal using a special atomizer using Ar gas and performing emission spectroscopic analysis (BISRA, Annual Report: 78 (1966), 65,
Research and development has been attempted using various methods such as 78 (1967) and 35 (1968)). However, these methods have never been actually put into practical use at a manufacturing site and have only been attempted on a laboratory scale.
実際の製造現場で実用可能な溶融金属の直接分
析装置の実現をはかるには、先ず、その製造現場
は高温、振動、ダストなど測定環境が非常に悪い
点を考慮しなければならない。このような劣悪な
測定環境下ではトラブルが起る分光、検出器等の
精密測定機器は、溶融金属の存在場所から離して
設置し、溶融金属は、電気的放電などによつて微
粉化して搬送するなどの方法が有望になる。 In order to create a direct analysis device for molten metal that can be put to practical use at actual manufacturing sites, it must first be taken into account that the manufacturing site has a very poor measurement environment, including high temperatures, vibrations, and dust. Precision measuring instruments such as spectrometers and detectors, which can cause problems in such poor measurement environments, should be installed away from the molten metal, and the molten metal should be pulverized by electrical discharge before being transported. The following methods are promising.
本発明者らは、溶融金属を0.1μm以下で、粒度
分布域が狭い超微粒子を安定して発生させる方
法、搬送管内壁への微粒子の付着残留を防止して
数10mの長距離を効率よく搬送する方法及び分析
装置への導入方法等を中心に研究開発を進め、簡
単迅速に高い精度感度で分析でき、実用的な新規
分析装置を提供するにいたつたものである。 The present inventors have developed a method to stably generate ultrafine particles with a narrow particle size distribution range of 0.1 μm or less from molten metal, and to efficiently cover long distances of several tens of meters by preventing fine particles from adhering to the inner wall of the conveying pipe. We have conducted research and development focusing on transportation methods and methods of introduction into analytical equipment, and have now provided a practical new analytical equipment that can be analyzed simply, quickly, and with high precision and sensitivity.
第1図、第2図に示す本発明実施例装置によ
り、本発明の詳細について説明する。 The details of the present invention will be explained using an embodiment of the present invention shown in FIGS. 1 and 2.
本発明装置は、大別すると微粒子生成プローブ
1、湯面レベル計38と連動する同プローブの上
下位置調節装置20、深層部の溶融金属をプロー
ブ下部に取り込む耐火物円筒39、スパーク放電
装置18、微粒子搬送管22、搬送ガス分配装置
24及びプラズマ励起源を有する発光分光分析装
置37から構成される。微粒子生成プローブ1
は、溶融金属13と対電極8間に高電圧をかけて
スパーク放電を行わせ、溶融金属を局部的に更に
高温の過熱状態に保ち、金属の組成を代表する微
粒子を煙状に蒸発させる働きをする部分である。
対電極8は、先端をとがらせた2〜5mmφ程度の
小径の丸棒が適切であり、材質は蒸発消耗の少な
い高融点金属であるタングステンなどが適してい
る。先端を円錐状にとがらせた形状は、微粒子を
常時一定速度で蒸発させる上で重要である。 The device of the present invention can be roughly divided into a particulate generation probe 1, a vertical position adjustment device 20 for the probe that works in conjunction with a hot water level gauge 38, a refractory cylinder 39 that takes molten metal from deep into the lower part of the probe, a spark discharge device 18, It is composed of a particle transport pipe 22, a carrier gas distribution device 24, and an emission spectrometer 37 having a plasma excitation source. Fine particle generation probe 1
The function is to apply a high voltage between the molten metal 13 and the counter electrode 8 to cause a spark discharge, keep the molten metal locally in a superheated state at a higher temperature, and evaporate fine particles representing the composition of the metal in the form of smoke. This is the part that does this.
The counter electrode 8 is suitably a round bar with a small diameter of about 2 to 5 mm with a pointed tip, and the suitable material is tungsten, which is a high melting point metal with little evaporation consumption. The conical shape of the tip is important for evaporating fine particles at a constant rate.
対電極8先端部と溶融金属13表面との間隙を
5mmとして、スパーク放電を飛ばすと約10mmφの
範囲内でパルス放電が繰り返され、放電カラム1
4も安定して形成され、微粒子の蒸発量も常時安
定し、良好な分析結果が得られる。湯面レベルが
多小変動しても、常に対電極先端からの放電カラ
ム14が形成され、微粒子の蒸発量の変動もごく
わずかに抑えることができた。電極間間隙を5mm
に設定した場合、±2mmの湯面の変動が起つても、
微粒子の生成量の変動は5%以内に抑制できた。 When the gap between the tip of the counter electrode 8 and the surface of the molten metal 13 is set to 5 mm, and a spark discharge is caused, the pulse discharge is repeated within a range of about 10 mmφ, and the discharge column 1
4 is also stably formed, the amount of evaporation of fine particles is always stable, and good analytical results can be obtained. Even if the hot water level fluctuated a little, a discharge column 14 was always formed from the tip of the counter electrode, and fluctuations in the amount of evaporation of fine particles could be suppressed to a very small amount. 5mm gap between electrodes
When set to , even if the hot water level fluctuates by ±2 mm,
Fluctuations in the amount of fine particles produced could be suppressed to within 5%.
しかし、対電極先端を丸棒の断面としたり、微
粒子導入管3のパイプ断面を直接電極先端として
用いた場合は、安定した放電カラムが形成され
ず、とくに湯面の変動が起つた場合は放電カラム
が移動し、微粒子の蒸発量の再現性が得られなく
なり、分析精度を極端に低下させた。 However, if the tip of the counter electrode is a cross section of a round bar or the cross section of the pipe of the particle introduction tube 3 is directly used as the tip of the electrode, a stable discharge column will not be formed, and especially if the melt level fluctuates, the discharge The column moved, and the reproducibility of the amount of evaporated particles could no longer be obtained, resulting in an extremely low analytical accuracy.
このような理由から、微粒子導入管3は対電極
8の電導体としては用いるが、スパーク放電用の
対電極は、この導入管3の先端に固設するように
した。この固設の方法はいくつかあるが、第2図
に示すように、微粒子導入管3の下端に円筒状の
電極ホルダー6を溶接などによつて接続し、電極
ホルダー6の中心部に対電極8を垂直に挿入し、
微粒子導入口7を開けるようにして、ビス9など
で固定する方法が適当である。 For these reasons, the particle introduction tube 3 is used as a conductor for the counter electrode 8, but the counter electrode for spark discharge is fixed at the tip of the introduction tube 3. There are several methods for fixing this, but as shown in Figure 2, a cylindrical electrode holder 6 is connected to the lower end of the particle introduction tube 3 by welding or the like, and a counter electrode is attached to the center of the electrode holder 6. Insert 8 vertically,
A suitable method is to open the particle inlet 7 and fix it with screws 9 or the like.
微粒子導入管3は、鋼や銅製の内径2〜3mmφ
程度の小径の管を用いるが、上部は耐熱絶縁材を
介して冷却筒2頂部に固定保持される。微粒子導
入管3の外側には、アルミナやマグネシアなどの
耐熱絶縁管4が被覆されるが、その外周には同心
円状にわずかな間隙5ができるように、冷却筒2
内部には穴があけられており、この間隙5の上部
はArなどの不活性ガス供給管15が取りつけら
れ、下部はガス吹き出し口10につながつてい
る。 The particle introduction pipe 3 is made of steel or copper and has an inner diameter of 2 to 3 mmφ.
A pipe with a relatively small diameter is used, and the upper part is fixedly held at the top of the cooling cylinder 2 via a heat-resistant insulating material. The outside of the particulate introduction tube 3 is coated with a heat-resistant insulating tube 4 made of alumina, magnesia, etc., and the cooling tube 2 is coated with a small gap 5 concentrically around the outer circumference.
A hole is made inside, and an inert gas supply pipe 15 such as Ar is attached to the upper part of this gap 5, and the lower part is connected to a gas outlet 10.
冷却筒2自体は、溶融金属の副射熱による加熱
を防止するために、空冷あるいは水冷によつて冷
却できる機構を備えている。又、冷却筒2の下部
周囲には窒化ホウ素などの絶縁耐火材でできた円
筒11が取り付けられており、下端を溶融金属1
3中に浸漬して内部に小空間室12を形成してい
る。 The cooling cylinder 2 itself is equipped with a mechanism capable of being cooled by air cooling or water cooling in order to prevent heating of the molten metal due to side radiation heat. Further, a cylinder 11 made of an insulating refractory material such as boron nitride is attached around the lower part of the cooling cylinder 2, and the lower end is connected to the molten metal 1.
3 to form a small space chamber 12 inside.
上記の微粒子導入管3の下端に、対電極8を取
り付けた電極ホルダー部6は、この小空間室12
につきでており、対電極8の先端部は溶融金属1
3表面に垂直に対向し、5〜10mmの範囲で一定間
隔をもつて設定され、対電極先端部のわずか上部
に、微粒子導入口7が下向きに開口している。ガ
ス吹き出し口10は小空間室12の頂部に位置
し、微粒子導入口7よりも上部位置にある方が、
蒸発した微粒子の効率的導入に適している。 The electrode holder part 6 with the counter electrode 8 attached to the lower end of the particle introduction tube 3 is connected to the small space chamber 12.
The tip of the counter electrode 8 is exposed to the molten metal 1.
The microparticle inlets 7 are perpendicularly opposed to the surfaces of the electrodes 3 and are set at regular intervals in the range of 5 to 10 mm, and slightly above the tip of the counter electrode, a particle inlet 7 is opened downward. The gas outlet 10 is located at the top of the small space chamber 12, and if it is located above the particle inlet 7,
Suitable for efficient introduction of evaporated fine particles.
対電極8先端部と溶融金属13表面間に高電圧
をかけて、スパーク放電を飛ばし、蒸発生成した
溶融金属の超微粒子は、Arガス吹き出し口10
から吐出したArガス流に乗つて、対電極8先端
直上に位置する微粒子導入口7に迅速に運び込ま
れる。小空間室12は直径30mmφ、高さ30mm以下
の小容積であり、蒸発微粒子の拡散は起りにく
く、生成すると同時に効率よく導入口7へ導入さ
れる。吹き込まれる不活性ガスは、小空間室12
内の大気を追い出してスパーク放電が起り易い雰
囲気をつくるためと、生成した微粒子を分析計へ
搬送するために必要となる。 A high voltage is applied between the tip of the counter electrode 8 and the surface of the molten metal 13 to cause spark discharge, and the ultrafine particles of the evaporated molten metal are collected at the Ar gas outlet 10.
The particles are quickly carried into the particle introduction port 7 located directly above the tip of the counter electrode 8 by riding on the Ar gas flow discharged from the counter electrode 8 . The small space chamber 12 has a small volume with a diameter of 30 mmφ and a height of 30 mm or less, so that diffusion of evaporated particles is difficult to occur, and as soon as they are generated, they are efficiently introduced into the introduction port 7. The inert gas blown into the small space chamber 12
This is necessary to expel the atmosphere inside the tank to create an atmosphere conducive to spark discharge, and to transport the generated particulates to the analyzer.
ガスの種類は、生成する微粒子の粒径や量に影
響し、Ar,He,Ar―H2などが用いられるが、
通常はArガスが適当である。生成した微粒子の
拡散を防ぐために、放電を行う空間室12を極力
小さくする必要があるが、そのために通常10〜20
/minで吹き込まれるArガスによつて溶融金
属表面が冷却される弊害が起り易くなる。微粒子
を伴なつて導入管3を通過するArガス温度は数
100度に達するが、本発明のArガスの吹き込み
は、導入管3の外壁に作つた間隙5を通つて供給
されるために、熱交換作用によつて予熱されてか
ら吹き込まれるので、溶融金属表面の冷却は防止
できる。 The type of gas affects the particle size and amount of fine particles generated, and Ar, He, Ar-H2, etc. are used.
Ar gas is usually suitable. In order to prevent the dispersion of the generated fine particles, it is necessary to make the space chamber 12 in which the discharge occurs as small as possible.
The molten metal surface is likely to be cooled by the Ar gas blown in at a rate of /min. The temperature of the Ar gas passing through the introduction pipe 3 with fine particles is several
Although the temperature reaches 100 degrees, Ar gas according to the present invention is supplied through the gap 5 made on the outer wall of the introduction pipe 3, so it is preheated by heat exchange before being blown into the molten metal. Cooling of the surface can be prevented.
又、蒸発生成した超微粒子は、管内壁の温度が
低いと即座に内壁に付着する性質をもち、微粒子
の定量的な搬送が困難になる。あるいは、微粒子
搬送管22を数10mのように長尺とした場合に起
り易くなる管内などに付着残留する微粒子を洗浄
する目的で、断続的に高圧をかけてArガスを高
速で吹き込む必要がある。これらの目的から冷却
筒2内に設ける微粒子導入管3は、冷却筒2に直
接接触して冷却されず、またArガス吹き込み間
隙5は極力狭くするとともに、ガスが導入管3外
壁に効率よく接触するように、微粒子導入管3の
外側に狭い間隙をもつて同心円状に2重管構造と
することが必要である。 Further, the ultrafine particles produced by evaporation have a property of immediately adhering to the inner wall of the tube when the temperature of the inner wall is low, making it difficult to quantitatively transport the fine particles. Alternatively, it is necessary to intermittently apply high pressure and blow Ar gas at high speed in order to clean the particulates that adhere and remain inside the pipe, which tends to occur when the particulate transport pipe 22 is made long, such as several tens of meters. . For these purposes, the particulate introduction pipe 3 installed in the cooling cylinder 2 is not cooled by directly contacting the cooling cylinder 2, and the Ar gas injection gap 5 is made as narrow as possible, so that the gas can efficiently contact the outer wall of the introduction pipe 3. In order to do this, it is necessary to form a concentric double pipe structure with a narrow gap on the outside of the particle introduction pipe 3.
また、長時間連続して放電を飛ばしていると、
対電極8の先端部に蒸発生成した微粒子の一部が
付着してくるために、断続的に極性を逆にして放
電させ、付着した微粒子を蒸発除去するなどの方
法をとる。しかし、長時間連続分析の場合には、
対電極の交換が必要になる。この交換は迅速に行
わなければならないが、本発明では対電極8と微
粒子導入管3を一体化してあるために、冷却筒2
上部の固定具を取りばずして、上方に引きぬく簡
単な操作で迅速に交換できる利点がある。 Also, if the discharge continues for a long time,
Since some of the evaporated particles adhere to the tip of the counter electrode 8, a method is used in which the polarity is intermittently reversed and discharge is performed to evaporate and remove the attached particles. However, in the case of long-term continuous analysis,
The counter electrode will need to be replaced. This replacement must be done quickly, but since the counter electrode 8 and the particle introduction tube 3 are integrated in the present invention, the cooling cylinder 2
It has the advantage that it can be replaced quickly by simply removing the upper fixture and pulling it upwards.
溶融金属を直接分析する場合にもつとも問題に
なるのは、湯面のレベル変動が激しいことで、レ
ベルが静止状態にあるものはまれである。すなわ
ち、成分含有率を知る分析の目的は、金属製造の
工程管理であるために、製造過程での直接分析が
必要であり、製造過程における溶融金属湯面は通
常安定していない。鉄鋼製造を例にとれば、溶鉱
炉から樋に流れ出てくる溶銑は時々刻々湯の量が
変化するし、そのあとの鍋中で行う脱リン、脱
硫、脱炭などの処理では、湯面の変動は激しく沸
とう状態を呈している。機械的な工夫や比較的安
定している時期を選んで分析を実施することにし
ても、スパーク放電によつて微粒子を蒸発生成す
るときの対電極8先端と溶融金属13表面との間
隙は、通常10mm以下にする必要があるために、湯
面レベル変動の対策が必須になる。 A problem with directly analyzing molten metal is that the level of the molten metal fluctuates dramatically, and it is rare for the level to remain static. That is, since the purpose of analysis to know the component content is process control of metal manufacturing, direct analysis during the manufacturing process is necessary, and the molten metal level during the manufacturing process is usually not stable. Taking steel manufacturing as an example, the amount of hot metal that flows from the blast furnace into the gutter changes from moment to moment, and during subsequent processes such as dephosphorization, desulfurization, and decarburization in the ladle, changes in the level of the hot metal occur. is in a state of intense boiling. Even if the analysis is carried out by mechanical means or by selecting a relatively stable period, the gap between the tip of the counter electrode 8 and the surface of the molten metal 13 when fine particles are evaporated and generated by spark discharge is Since it usually needs to be 10mm or less, it is essential to take measures against fluctuations in the level of the hot water.
そこで、本発明では第1図に示すように、湯面
レベル検出器38を溶融金属13表面に対向して
設置し、湯面レベルを常時検出し、この検出信号
によつて対電極8を保持した微粒子生成プローブ
1の冷却筒2を、上下に駆動する上下位置調節装
置20を作動させて、対電極と溶融金属間の電極
間間隙を一定間隔に保持する方法をとつた。 Therefore, in the present invention, as shown in FIG. 1, a hot water level detector 38 is installed facing the surface of the molten metal 13 to constantly detect the hot water level and use this detection signal to hold the counter electrode 8. A method was adopted in which a vertical position adjustment device 20 for vertically driving the cooling cylinder 2 of the fine particle generation probe 1 was operated to maintain the interelectrode gap between the counter electrode and the molten metal at a constant interval.
湯面レベル検出器は、静電容量型などのものが
適当であるが、微粒子生成プローブ1あるいは同
プローブの支持架台19などに固定保持する。同
プローブ1の上下動の駆動源20は、電動機及び
スクリユージヤツキ等を用い、同プローブの上部
に取り付ける。湯表面の小きざみなレベル変動
は、耐火筒11を溶融金属中に浸漬して、小空間
室12を形成することによりかなり消失するが、
湯面レベル計38によるレベル検出精度は±0.5
mm以上で、検出信号を上下動動作に変換する速度
も速く、本方式によれば電極間間隙を常時5mm±
1mmに調節することができ、微粒子の生成を安定
して行え良好な精度で分析を実施することが可能
になつた。 The hot water level detector, which is suitably of a capacitance type, is fixedly held on the particulate generation probe 1 or the supporting frame 19 of the probe. A driving source 20 for vertical movement of the probe 1 is attached to the top of the probe using an electric motor, screw jack, etc. Small level fluctuations on the hot water surface can be largely eliminated by immersing the refractory tube 11 in the molten metal to form the small space chamber 12;
The level detection accuracy by the hot water level meter 38 is ±0.5
mm or more, the speed at which the detection signal is converted into vertical motion is fast, and according to this method, the gap between the electrodes is always 5 mm ±
It has become possible to adjust the diameter to 1 mm, stably generate fine particles, and conduct analysis with good accuracy.
溶融金属の直接分析におけるもう一つの大きな
問題は、溶融金属表面に浮上するスラグの排除及
び深層部溶接金属の微粒子生成プローブ内への取
り込みである。溶融金属表面には通常スラグが浮
上していたり、酸化被膜が生成しており、分析に
当つてはこれらを排除して、溶融金属表面を露出
させる必要がある。また、スラグ層直下の溶融金
属は、スラグ―メタル反応による影響で、更に深
部の溶融金属の成分組成と異なる場合が多く、ス
ラグを排除すると共に、更に深層部の溶融金属を
分析対象にする必要がある。 Another major problem in direct analysis of molten metal is the elimination of slag that floats to the surface of the molten metal and the incorporation of deep weld metal into the particulate-generating probe. Usually, slag floats on the surface of the molten metal, and an oxide film is formed, and for analysis, it is necessary to remove these and expose the surface of the molten metal. Furthermore, the composition of the molten metal directly under the slag layer is often different from that of the molten metal in the deeper layer due to the influence of the slag-metal reaction, so it is necessary to eliminate the slag and also analyze the molten metal in the deeper layer. There is.
本発明では、第1図に示すように、微粒子生成
プローブ1及び湯面レベル計38を内包し、下端
に対象とする溶融金属と同等ないしはより低い融
点の材料でできたキヤツプ41をかぶせたスラグ
遮へい用耐火物製円筒39を、溶融金属13中に
浸入させる方法をとつた。マグネシア、アルミ
ナ、窒化ホウ素などの耐火材で製作した円筒39
の上部には、昇降装置40が取り付けてあり、分
析開始前は同耐火円筒39は微粒子生成プローブ
1と同様に、溶融金属の上方に引き上げられてい
るが、最初にスラグ遮へい用耐火円筒39を下降
させ、スラグ層42を通過してスラグを排除し、
溶融金属13中に浸入させる。 In the present invention, as shown in FIG. 1, a slag containing a particulate generation probe 1 and a molten metal level gauge 38, and a cap 41 made of a material having a melting point equal to or lower than that of the target molten metal is covered at the lower end. A method was adopted in which a shielding refractory cylinder 39 was infiltrated into the molten metal 13. Cylinder 39 made of refractory materials such as magnesia, alumina, and boron nitride.
A lifting device 40 is attached to the top of the slag shielding cylinder 39. Before starting analysis, the refractory cylinder 39 is lifted above the molten metal in the same way as the particle generation probe 1. lowering and passing through the slag layer 42 to remove the slag,
Infiltrate into the molten metal 13.
底部に取り付けたキヤツプ41は、溶融金属1
3によつて溶解され、深層部の溶融金属が耐火円
筒39の内部に取り入れられる。このあとに、微
粒子生成プローブ1を下降させて分析を開始す
る。分析終了後は、耐火円筒39を微粒子生成プ
ローブ1と共に引き上げ、耐火円筒39の下端に
は、新しいキヤツプ41を取り付けて次の分析に
待機する。 The cap 41 attached to the bottom holds the molten metal 1.
3, and the molten metal in the deep layer is taken into the refractory cylinder 39. After this, the particle generation probe 1 is lowered to start analysis. After the analysis is completed, the refractory cylinder 39 is pulled up together with the particle generation probe 1, and a new cap 41 is attached to the lower end of the refractory cylinder 39, waiting for the next analysis.
すなわち、キヤツプ41は消耗品として使用す
るので交換が容易な必要があるが、円筒39の下
端にかるくはめ込む装着方法でよかつた。このキ
ヤツプ41は溶融金属13によつて溶解されて分
析の対象になるが、耐火円筒39内に取り込まれ
る溶融金属の全体量に比べて、キヤツプ41の量
はわずかなためにほとんど問題にならないが、な
るべく分析対象成分を含まない材料を用いる。 That is, since the cap 41 is used as a consumable item, it needs to be easy to replace, but it can be attached by fitting it lightly into the lower end of the cylinder 39. This cap 41 is melted by the molten metal 13 and becomes the subject of analysis, but since the amount of the cap 41 is small compared to the total amount of molten metal taken into the refractory cylinder 39, it is hardly a problem. If possible, use materials that do not contain the component to be analyzed.
溶融金属中に溶け込むキヤツプの量を減少する
ため及びキヤツプの機械的強度を増加するために
は、耐火円筒39の底部を耐火材でおおい、中央
に小穴を開け、その外側にキヤツプをかぶせるな
どの方法が有効であつた。上記の本発明の方法に
よれば、スラグは十分に排除でき、深層部溶融金
属の採取も良好に行われた。 In order to reduce the amount of cap that dissolves into the molten metal and to increase the mechanical strength of the cap, it is possible to cover the bottom of the refractory cylinder 39 with a refractory material, make a small hole in the center, and cover the outside with the cap. The method was effective. According to the method of the present invention described above, slag could be sufficiently removed and deep molten metal could be collected satisfactorily.
溶融金属13を微粒子に変換する方法は種々あ
るが、前述の引用文献のように、高速のArガス
流によるスプレー作用で噴霧する方法では、生成
した微粒子径は10〜100μm程度以上で粒径が大
きいために長距離搬送は困難であり、又粒度分布
の幅が大きいために励起発光させた際の発光強度
の変動が大きく、分析精度が悪い等の問題があ
る。直流アークあるいはアークカラムを、水冷に
よるピンチ効果で収束したプラズマアーク照射に
よる過熱蒸発による方法では、対電極と溶融金属
表面との電極間ギヤツプを、1〜2mm程度の極め
て短かい距離に保たなければ、ある一定量以上の
微粒子の蒸発が起らず、かつ蒸気圧の低い成分の
蒸発が優先するいわゆる選択蒸発が起り易く、溶
融金属の成分組成を代表する微粒子を安定して生
成させることが難かしい。 There are various methods of converting molten metal 13 into fine particles, but in the method of atomizing by a spray action using a high-speed Ar gas flow, as in the above-mentioned cited document, the fine particles generated are approximately 10 to 100 μm or more in diameter. Because of their large size, it is difficult to transport them over long distances, and because their particle size distribution is wide, the emission intensity fluctuates greatly when excited and emitted, leading to problems such as poor analysis accuracy. In the method of superheating evaporation by direct current arc or arc column irradiation with plasma arc converged by the pinch effect of water cooling, the interelectrode gap between the counter electrode and the molten metal surface must be kept at an extremely short distance of about 1 to 2 mm. For example, so-called selective evaporation is likely to occur, in which the evaporation of fine particles exceeding a certain amount does not occur and the evaporation of components with low vapor pressure takes priority, and it is difficult to stably generate fine particles that are representative of the component composition of the molten metal. It's difficult.
レーザー照射による方法は、非導電性物質に適
用できる利点をもつが、CO2レーザーのように連
続レーザーでは蒸発量が少なく、ジヤイアントパ
ルスレーザーを採用せざるを得ないが、1秒間に
数10回以上での高出力での照射が不可能なことか
ら、これもまた正確なオンライン分析用にはあま
り適当でない。 Methods using laser irradiation have the advantage of being applicable to non-conductive materials, but continuous lasers such as CO 2 lasers have a small amount of evaporation, so a giant pulse laser has to be used, but the evaporation rate is several tens of tens of times per second. This is also not very suitable for accurate on-line analysis since it is not possible to irradiate at high power for more than one time.
本発明者らは、溶融金属を微粒子として蒸発生
成するエネルギー源の適正について詳細な研究を
続けた結果、最適な方法としてスパーク放電を選
定した。すなわち、溶融金属13中に浸漬した炭
素や高融点金属から成る棒状電極17を試料極と
して陰極とし、溶融金属13表面に、先端がわず
かな間隙をもつて設置した対電極8に導通する微
粒子導入管3の上端に取り付けた端子16を陽極
として、スパーク放電装置18に結線し、両極に
高電圧をかけてスパーク放電を行い、溶融金属1
3を微粒子として蒸発させる。 The present inventors continued detailed research into the suitability of an energy source for vaporizing and generating molten metal as fine particles, and as a result, they selected spark discharge as the optimal method. That is, a rod-shaped electrode 17 made of carbon or high-melting point metal immersed in molten metal 13 is used as a sample electrode and a cathode, and fine particles are introduced whose tip is electrically connected to a counter electrode 8 installed on the surface of molten metal 13 with a slight gap. The terminal 16 attached to the upper end of the tube 3 is used as an anode, connected to a spark discharge device 18, and a high voltage is applied to both poles to generate a spark discharge, and the molten metal 1
3 is evaporated as fine particles.
溶融金属を微粒子として蒸発搬送し、溶融金属
中の各種含有成分量を分析するためには、含有成
分を代表する微粒子を安定して発生させることが
とくに重要であるが、スパーク放電における各放
電定数の設定の仕方も影響を与える。自己誘導
10μH、静電容量3μF、抵抗1Ω、電圧1000Vに設
定したスパークライクのスパーク放電と各定数を
150μH,8μF,0Ω,700Vに設定したアークライ
クのスパーク放電(放電電流波形からみると、前
者はピーク電流値200A、保持時間30μS、後者
各々が80A,400μS)の両放電条件で、鉄鋼試料
を対象に微粒子を発生させ、各成分を繰り返して
分析した結果、0.50%含有するSiの分析値の変動
係数は前者が2.5%、後者が11.6%,1.04%含有す
るMnは各々3.8%,12.6%,0.30%含有するCuは
各々5.1%,14.2%などの結果が得られた。 In order to evaporate and transport molten metal as fine particles and analyze the amount of various components contained in the molten metal, it is especially important to stably generate fine particles that represent the contained components. How it is set also has an impact. self-guided
Spark-like spark discharge and each constant set to 10μH, capacitance 3μF, resistance 1Ω, and voltage 1000V.
A steel sample was examined under both arc-like spark discharge conditions set at 150 μH, 8 μF, 0 Ω, and 700 V (as seen from the discharge current waveform, the former had a peak current of 200 A and a holding time of 30 μS, and the latter had a peak current of 200 A and a holding time of 30 μS, respectively). As a result of generating fine particles in the target and repeatedly analyzing each component, the coefficient of variation of the analysis value for Si containing 0.50% was 2.5% for the former, 11.6% for the latter, and 3.8% and 12.6% for Mn containing 1.04%, respectively. , 0.30% Cu content was obtained as 5.1% and 14.2%, respectively.
すなわち、上記のようにアークライクよりもス
パークライクのスパーク放電の方が、安定して溶
融金属の各成分を微粒子として蒸発させるのに適
している。放電周波数については、50〜800Hzま
でについて調べたが、200Hz以上のように、単位
時間当りの放電回数が多い方が分析精度の点から
有利であつた。 That is, as described above, spark-like spark discharge is more suitable for stably vaporizing each component of molten metal as fine particles than arc-like spark discharge. Regarding the discharge frequency, we investigated the range from 50 to 800 Hz, and it was found that a frequency of 200 Hz or higher, in which the number of discharges per unit time is large, is advantageous in terms of analysis accuracy.
溶融金属中の成分分析を目的とする本発明にお
いては、微粒子を単に生成する場合と異なり、蒸
発微粒子を一定流速の搬送ガスと共に、常時安定
して分析装置37へ送り込まねばならず、より効
率の良い微粒子の搬送技術が必要になる。本発明
では、溶融金属13表面より蒸発して対電極8先
端直上方向に立ち昇つた微粒子を、周囲への拡散
を防ぎ、Arガス吹き込み管5の下端部10より
吹き出して、微粒子導入管3下端の開口部7へ流
れ込むArガス流に乗せて迅速に運び去る方法を
とつた。 In the present invention, which aims at component analysis in molten metal, unlike the case where fine particles are simply generated, the evaporated fine particles must be constantly and stably fed to the analyzer 37 together with the carrier gas at a constant flow rate, resulting in a more efficient method. Good particle transport technology is required. In the present invention, the fine particles evaporated from the surface of the molten metal 13 and rising directly above the tip of the counter electrode 8 are prevented from diffusing to the surroundings, and are blown out from the lower end 10 of the Ar gas blowing tube 5 to the lower end of the fine particle introduction tube 3. A method was adopted in which the Ar gas flowing into the opening 7 of the Ar gas flow was carried away quickly.
微粒子が発生する小空間室12は微粒子導入管
3の開口部7以外に出口がないために、Arガス
流に引き込まれて、常時一定の希釈倍率をもつて
導入管3の開口部7へ送り込まれる。対電極8先
端部と溶融金属表面で形成する放電カラム14の
放電を乱さずに、かつ微粒子を安定して同開口部
7へ送り込むためのArガス流を形成するために
は、Arガス吹き出し用管5の下端の吹き出し口
10は、微粒子導入管3下端の開口部7よりも、
わずかに上部に位置する必要がある。 Since the small space chamber 12 in which the particles are generated has no outlet other than the opening 7 of the particle introduction tube 3, the particles are drawn into the Ar gas flow and sent into the opening 7 of the introduction tube 3 at a constant dilution ratio. It will be done. In order to form an Ar gas flow to stably send fine particles to the opening 7 without disturbing the discharge of the discharge column 14 formed by the tip of the counter electrode 8 and the surface of the molten metal, it is necessary to The outlet 10 at the lower end of the tube 5 is larger than the opening 7 at the lower end of the particle introduction tube 3.
It should be located slightly at the top.
微粒子導入管3に導入された微粒子は、Arガ
ス流に乗せられて、絶縁コネクター21によつて
接続される微粒子搬送管22を通つて、搬送ガス
分配装置24に搬送されるが、本発明のように微
粒子を対象に分析を行う場合には、これらの内壁
に微粒子を付着残留させないことが重要な問題に
なる。微粒子導入管3は、溶融金属の高熱によつ
て加熱されているので、微粒子は付着しにくくあ
まり問題はないが、搬送管22は距離が長くなる
と、温度が低下して付着残留が起り易くなる。そ
の結果、搬送ガス中の微粒子濃度が変動したり、
コンタミネーシヨンとなつて正確な分析値が得ら
れなくなる。 The particles introduced into the particle introduction pipe 3 are carried by the Ar gas flow and are transported to the carrier gas distribution device 24 through the particle transport pipe 22 connected by the insulating connector 21. When performing analysis on fine particles such as these, it is important to prevent the fine particles from remaining on the inner walls. Since the particulate introduction pipe 3 is heated by the high heat of the molten metal, it is difficult for the particulates to adhere to it and there is no problem, but as the distance of the transport pipe 22 becomes longer, the temperature decreases and it becomes easier for the particulates to remain attached. . As a result, the concentration of particulates in the carrier gas fluctuates,
Contamination occurs and accurate analysis values cannot be obtained.
従つて、搬送管22はなるべく小径として搬送
ガスの流速を速くする。図面に示す如く加熱装置
23を取り付けて、常時加熱しておくかあるいは
一度付着した微粒子は、付着後短時間以内では容
易に剥離できるので、搬送ガスを更に高速で吹き
込んで洗浄する方法などを採用した。 Therefore, the diameter of the transport pipe 22 is made as small as possible to increase the flow rate of the transport gas. As shown in the drawing, a heating device 23 is installed to heat the surface constantly, or fine particles once attached can be easily peeled off within a short period of time, so a method such as cleaning by blowing carrier gas at a higher speed is adopted. did.
搬送ガス分配装置24は、搬送管22より搬送
ガスで送られてきた微粒子を、一旦小空間部で拡
散させ更に均一化をはかる。プラズマトーチ29
へ導入する搬送ガスの最適流量を得るために、あ
る一定部分を系外に排出して搬送ガスの分配を行
う。あるいは搬送されてくる間に凝集が進んで、
特に粗大化した粒子を系外に排除して、微細粒子
のみをプラズマトーチ29へ送り込むための分粒
などを行うためのものである。 The carrier gas distribution device 24 once diffuses the fine particles sent by the carrier gas from the carrier pipe 22 in a small space to further make the particles uniform. plasma torch 29
In order to obtain the optimum flow rate of the carrier gas introduced into the system, the carrier gas is distributed by discharging a certain portion out of the system. Or, agglomeration progresses while being transported,
In particular, it is used to perform particle sizing, etc., in order to exclude coarse particles from the system and send only fine particles to the plasma torch 29.
分配装置24は、外周に加熱装置23を取り付
けた小径の円筒管で、微粒子搬送管22を側壁よ
り挿入して管末端開口部25を上向きに、微粒子
供給管26を、円筒管の上部より搬送管末端開口
部25と一定間隔をもつて、相対するように取り
付け、円筒管底部には、流量調節器28を備えた
排出管27を取り付けてある。この3本の管は、
いずれも10mmφ以下の細管で、粗大粒子及び余剰
の微粒子及び搬送ガスは、底部排出管27より系
外に排出され、残りの微粒子は一定流量の搬送ガ
スと共に、供給管26へ導入される。 The distribution device 24 is a small-diameter cylindrical tube with a heating device 23 attached to its outer periphery.The particle conveying tube 22 is inserted through the side wall, the tube end opening 25 is directed upward, and the particle supply tube 26 is conveyed from the top of the cylindrical tube. A discharge pipe 27 is attached to the bottom of the cylindrical tube so as to be opposite to the tube end opening 25 at a constant distance. These three tubes are
Both are thin tubes with a diameter of 10 mm or less, and coarse particles, excess fine particles, and carrier gas are discharged from the system through a bottom discharge pipe 27, and the remaining fine particles are introduced into the supply pipe 26 together with a constant flow rate of carrier gas.
微粒子供給管26は、プラズマ励起発光分光分
析装置37に接続される。導入された微粒子は図
示する如く、微粒子供給管26、プラズマガス供
給管30、冷却ガス供給管31から成る3重管の
プラズマトーチ29に運び込まれ、高周波発生装
置32によつて形成される高温のArプラズマ部
33に達して、励起発光される。励起光は分光器
34で分光され、光電子増倍管等から成る検出器
35、成分含有率算出装置36によつて、各々の
スペクトル線強度が測定され、溶融金属中の各成
分含有率を迅速に求められる。微粒子を励起発光
させる分析装置37としては、高周波誘導結合型
発光分光分析装置が最も適していたが、そのほか
の各種アーク放電等のプラズマ励起発光分光分析
装置あるいは原子吸光分析装置などを適用でき
る。 The particle supply pipe 26 is connected to a plasma excitation emission spectrometer 37 . As shown in the figure, the introduced particles are carried into a triple-tube plasma torch 29 consisting of a particle supply pipe 26, a plasma gas supply pipe 30, and a cooling gas supply pipe 31, and are heated to a high temperature generated by a high frequency generator 32. The light reaches the Ar plasma section 33 and is excited to emit light. The excitation light is separated into spectra by a spectrometer 34, and the intensity of each spectral line is measured by a detector 35 consisting of a photomultiplier tube or the like and a component content calculation device 36, which quickly calculates the content of each component in the molten metal. is required. Although a high-frequency inductively coupled emission spectrometer is most suitable as the analyzer 37 that excites the particles to emit light, other types of plasma-excited emission spectrometers such as arc discharge or atomic absorption spectrometers can be used.
本発明装置の分析操作について簡単に述べる。 The analysis operation of the apparatus of the present invention will be briefly described.
先ず、スラグ遮へい用耐火円筒39を、昇降装
置40によつてスラグ層42を通過して溶融金属
13中に下降させる。先端のキヤツプ41が溶解
して深層部の溶融金属13が円筒39内に取り入
れられる。次に支持架台19に駆動源20をもつ
て取り付けられた微粒子生成プローブ1を、Ar
ガス吹き込み管15にArガスを吹き込みながら、
溶融金属13表面に向つて下降させる。Arガス
吹き出し口10からArガスを吹き出させ、耐火
筒11内の大気を追いだしながら、耐火筒11下
端を溶融金属13中に浸漬し、小空間室12を密
閉状とする。対電極8先端部と溶融金属13表面
間は、湯面レベル計38と上下位置調節装置20
によつて、所定の間隔に自動的に調節され、スパ
ーク放電装置18の操作により、試料電極17と
対電極8間に高電圧をかけてスパーク放電を飛ば
す。 First, the slag shielding refractory cylinder 39 is lowered into the molten metal 13 through the slag layer 42 by the lifting device 40 . The cap 41 at the tip is melted and the molten metal 13 in the deep layer is taken into the cylinder 39. Next, the particle generation probe 1 attached to the support frame 19 with the drive source 20 is
While blowing Ar gas into the gas blowing pipe 15,
It is lowered toward the surface of the molten metal 13. While blowing out Ar gas from the Ar gas outlet 10 and expelling the atmosphere inside the refractory tube 11, the lower end of the refractory tube 11 is immersed in the molten metal 13 to seal the small space chamber 12. Between the tip of the counter electrode 8 and the surface of the molten metal 13, there is a level gauge 38 and a vertical position adjustment device 20.
By operating the spark discharge device 18, a high voltage is applied between the sample electrode 17 and the counter electrode 8 to generate a spark discharge.
蒸発生成した微粒子は微粒子導入管3、搬送管
22、ガス分配装置24を経てプラズマトーチ2
9に送り込まれ励起発光するが、10秒間程度の積
分発光強度値から各成分含有率を測定する。分析
終了後、微粒子生成プローブ1のArガス吹込み
管15からArガスを高圧で断続的に吹き込み微
粒子搬送管22内壁などに付着した微粒子を洗い
落す。 The evaporated particles are transferred to the plasma torch 2 via the particle introduction pipe 3, the transport pipe 22, and the gas distribution device 24.
9 to emit excited light, and the content of each component is measured from the integrated emission intensity value for about 10 seconds. After the analysis is completed, Ar gas is intermittently blown at high pressure from the Ar gas blowing pipe 15 of the particulate generation probe 1 to wash off the particulates adhering to the inner wall of the particulate transport pipe 22, etc.
次に耐火円筒39及び微粒子生成プローブ1を
溶融金属13よりひき上げ、再び分析する必要が
生じた時間に、先端に新らしいキヤツプを取り付
けた耐火円筒39を次にプローブ1を下降させ
て、上記操作を繰り返して、分析を実施する。生
成した微粒子の粒径及び粒度分布は、プラズマ中
で励起発光して分析する方法において、特に定量
精度に大きな影響を与えるので重要であるが、本
発明装置で、溶鋼を対象に発生させた微粒子は、
大略0.1μm以下の極めて微細粒子であり、平均粒
径が0.05μmの場合、0.04〜0.06μmの範囲に約70
%以上が入るように粒度分布の幅も狭く、プラズ
マ発光分光分析には最適であつた。 Next, the refractory cylinder 39 and the particulate generation probe 1 are pulled up from the molten metal 13, and when it becomes necessary to analyze again, the refractory cylinder 39 with a new cap attached to the tip is then lowered, and the probe 1 is lowered, and the probe 1 is lowered. Repeat the operation and perform the analysis. The particle size and particle size distribution of the generated fine particles are important because they have a large effect on the quantitative accuracy, especially in the method of analyzing by excitation and emission in plasma. teeth,
They are extremely fine particles of approximately 0.1 μm or less, and when the average particle size is 0.05 μm, there are approximately 70 particles in the range of 0.04-0.06 μm.
The width of the particle size distribution was narrow, so that the particle size distribution was more than %, making it ideal for plasma emission spectroscopic analysis.
以上説明したように本発明によれば、溶融金属
試料中の含有成分をサンプリング等の操作を行わ
ずに、迅速かつ精度よく直接分析することがで
き、金属の精錬や製鋼プロセスの操業管理に極め
て効果が大きい。 As explained above, according to the present invention, the components contained in a molten metal sample can be directly analyzed quickly and accurately without sampling or other operations, making it extremely useful for operational management of metal refining and steelmaking processes. Great effect.
第1図は本発明実施例装置全体の説明図、第2
図は微粒子生成プローブ先端部の説明図である。
1:微粒子生成プローブ、2:冷却筒、3:微
粒子導入管、5,15:Arガス吹込み管、8:
対電極、11:耐火筒、12:小空間室、13:
試料電極、17:試料電極、18:スパーク放電
装置、20:プローブ上下位置調節装置、22:
微粒子搬送管、24:搬送ガス分配装置、29:
プラズマトーチ、37:プラズマ発光分光分析装
置、38:湯面レベル計、39:スラグ遮へい用
耐火円筒、41:キヤツプ、42:スラグ。
Fig. 1 is an explanatory diagram of the entire apparatus according to the present invention;
The figure is an explanatory view of the tip of the particle-generating probe. 1: Particulate generation probe, 2: Cooling cylinder, 3: Particulate introduction pipe, 5, 15: Ar gas blowing pipe, 8:
Counter electrode, 11: Fireproof cylinder, 12: Small space chamber, 13:
Sample electrode, 17: Sample electrode, 18: Spark discharge device, 20: Probe vertical position adjustment device, 22:
Particulate transport pipe, 24: Carrier gas distribution device, 29:
Plasma torch, 37: Plasma emission spectrometer, 38: Hot water level meter, 39: Fireproof cylinder for slag shielding, 41: Cap, 42: Slag.
Claims (1)
融金属表面に対向して垂直に取り付けるとともに
同対電極の直上部に微粒子導入用の開口部を設
け、かつ、上端が微粒子搬送管に接続していると
ころの、同対電極の導電体を兼ねる細径で縦長形
状の微粒子導入管と、同微粒子導入管の外周に同
心円状になり、上部には供給口、下端には吐出口
を有する不活性ガス吹込管を介して、同導入管を
内包して保持し、周囲に冷却構造を備えた冷却筒
と、同冷却筒の下部周囲に、分析時には下端を溶
融金属中に浸漬して、内部に密閉状の小空間室を
形成するように設置した耐火筒とからなる微粒子
生成プローブ;上記微粒子導入管上部と、溶融金
属中に浸漬した試料電極とをそれぞれ接続したス
パーク放電装置;溶融金属表面に対向し、上記微
粒子生成プローブないしはプローブの支持架台に
固設した湯面レベル計の検出信号と連動して、対
電極先端部と溶融金属表面間の電極間隙を所望寸
法に制御する働きを持ち、同プローブ上部に取り
付けられた上下位置調整装置;上記微粒子生成プ
ローブ及び湯面レベル計を内包し、底部に対象と
する溶融金属と同等ないしはより低融点の材質か
らなるキヤツプを取り付けてあり、分析時に溶融
金属の深層部に侵入可能の長さを有して、上下動
の駆動装置を設備したスラグ遮へい用耐火物制円
筒;上記微粒子導入管上端と接続した微粒子搬送
管の末端部と、微粒子供給管の下端部と、余剰搬
送ガスの排出管とをとり付けた小形状容器からな
る搬送ガス分配装置;同微粒子供給管の末端部を
接続した高周波誘導結合型プラズマ等のプラズマ
励起源を有する発光装置と、分光器と、検出器と
を備えた発光分光分析装置;とから構成したこと
を特徴とする溶融金属の直接分析装置。1 At the lower end, a round rod counter electrode with a conical tip is attached vertically facing the molten metal surface, and an opening for introducing particles is provided directly above the counter electrode, and the upper end is connected to the particle transport pipe. It is connected to a small-diameter, vertically-shaped particulate introduction tube that also serves as a conductor for the counter electrode, and a concentric circle around the outer circumference of the same particulate introduction tube, with a supply port at the top and a discharge port at the bottom end. The introduction tube is enclosed and held through an inert gas blowing tube, and a cooling cylinder with a cooling structure is placed around the cooling cylinder, and the lower end of the cooling cylinder is immersed in the molten metal during analysis. , a particle generation probe consisting of a refractory cylinder installed to form a small sealed space inside; a spark discharge device in which the upper part of the particle introduction pipe and a sample electrode immersed in molten metal are respectively connected; A function that controls the electrode gap between the tip of the counter electrode and the molten metal surface to a desired dimension in conjunction with the detection signal of the hot water level meter that faces the metal surface and is fixed to the fine particle generation probe or the support frame of the probe. It has a vertical position adjustment device attached to the top of the probe; it contains the above-mentioned particle generation probe and liquid level gauge, and a cap made of a material with a melting point equal to or lower than that of the target molten metal is attached to the bottom. , a refractory cylinder for slag shielding, which has a length that allows it to penetrate deep into the molten metal during analysis, and is equipped with a vertical movement drive; the end of the particle transport pipe connected to the upper end of the particle introduction pipe; , a carrier gas distribution device consisting of a small container to which the lower end of a particulate supply pipe and a discharge pipe for excess carrier gas are attached; a plasma excitation source such as high-frequency inductively coupled plasma connected to the end of the particulate supply pipe; 1. A direct analysis device for molten metal, comprising: a light emitting device having a light emitting device; an emission spectrometer having a spectrometer; and a detector.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3077683A JPS59157539A (en) | 1983-02-28 | 1983-02-28 | Direct analyzer of molten metal in deep layer by fine particle generating plasma emission spectrochemical method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3077683A JPS59157539A (en) | 1983-02-28 | 1983-02-28 | Direct analyzer of molten metal in deep layer by fine particle generating plasma emission spectrochemical method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59157539A JPS59157539A (en) | 1984-09-06 |
| JPH0149891B2 true JPH0149891B2 (en) | 1989-10-26 |
Family
ID=12313082
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3077683A Granted JPS59157539A (en) | 1983-02-28 | 1983-02-28 | Direct analyzer of molten metal in deep layer by fine particle generating plasma emission spectrochemical method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59157539A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4615225A (en) * | 1985-03-13 | 1986-10-07 | Allied Corporation | In-situ analysis of a liquid conductive material |
| JPH02183144A (en) * | 1989-01-09 | 1990-07-17 | Nippon Steel Corp | Direct analysis on molten metal |
| JPH03261847A (en) * | 1990-03-12 | 1991-11-21 | Nippon Steel Corp | Fine particle forming probe for directly analyzing molten metal |
| US12584862B2 (en) | 2021-08-05 | 2026-03-24 | National Research Council Of Canada | Refractory lance assembly and refractory lance tube |
-
1983
- 1983-02-28 JP JP3077683A patent/JPS59157539A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59157539A (en) | 1984-09-06 |
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