JPS6321864B2 - - Google Patents
Info
- Publication number
- JPS6321864B2 JPS6321864B2 JP55083072A JP8307280A JPS6321864B2 JP S6321864 B2 JPS6321864 B2 JP S6321864B2 JP 55083072 A JP55083072 A JP 55083072A JP 8307280 A JP8307280 A JP 8307280A JP S6321864 B2 JPS6321864 B2 JP S6321864B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- oxygen
- tube
- reaction tube
- inert gas
- 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
Links
- 239000007789 gas Substances 0.000 claims description 33
- 229910000831 Steel Inorganic materials 0.000 claims description 32
- 239000010959 steel Substances 0.000 claims description 32
- 238000000034 method Methods 0.000 claims description 29
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 26
- 239000001301 oxygen Substances 0.000 claims description 26
- 229910052760 oxygen Inorganic materials 0.000 claims description 26
- 238000006243 chemical reaction Methods 0.000 claims description 24
- 239000011261 inert gas Substances 0.000 claims description 23
- 238000005070 sampling Methods 0.000 claims description 20
- 239000000523 sample Substances 0.000 claims description 15
- 238000004458 analytical method Methods 0.000 claims description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 9
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- 239000003575 carbonaceous material Substances 0.000 claims description 8
- 230000009970 fire resistant effect Effects 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 5
- 238000002844 melting Methods 0.000 description 4
- 230000008018 melting Effects 0.000 description 4
- 230000001105 regulatory effect Effects 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000004868 gas analysis Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000012024 dehydrating agents Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000004445 quantitative analysis Methods 0.000 description 2
- 239000010453 quartz Substances 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000007784 solid electrolyte Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 238000009628 steelmaking Methods 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910001030 Iron–nickel alloy Inorganic materials 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 238000000516 activation analysis Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 239000002775 capsule Substances 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000011978 dissolution method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- -1 oxides Chemical compound 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 238000010079 rubber tapping Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/20—Metals
- G01N33/205—Metals in liquid state, e.g. molten metals
Landscapes
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Medicinal Chemistry (AREA)
- Physics & Mathematics (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Investigating And Analyzing Materials By Characteristic Methods (AREA)
Description
【発明の詳細な説明】
この発明は、製鋼現場において溶解炉あるいは
取鍋内の溶鋼中に溶存する全酸素量を直接に、其
の場で、迅速且つ簡便に、測定する方法及び装置
に関するものである。[Detailed Description of the Invention] The present invention relates to a method and apparatus for directly, on-site, quickly and simply measuring the total amount of oxygen dissolved in molten steel in a melting furnace or ladle at a steelmaking site. It is.
一般に、鋼中には酸化物を含む酸素が例えば
SiO2,MnO,FeO等の種々な形で含まれている
が、これらの酸素が鋼中に多く残留すると展延性
等、熱間、冷間の加工性を劣化させ、また材料表
面の地疵の原因等となつて悪影響があるので、有
害酸素を低減させ調整するための脱酸処理が製鋼
工程で行われる。若し溶鋼中の酸素量が溶解炉や
取鍋等において炉前で直接測定できるならば、脱
酸などの操業上で得られる便益は大きい。 In general, steel contains oxygen containing oxides, such as
Oxygen is contained in various forms such as SiO 2 , MnO, and FeO, but if a large amount of these oxygen remains in steel, it deteriorates ductility and hot and cold workability, and also causes scratches on the material surface. Since harmful oxygen has an adverse effect, such as causing harmful oxygen, deoxidation treatment is performed in the steelmaking process to reduce and control harmful oxygen. If the amount of oxygen in molten steel could be directly measured in front of a melting furnace, ladle, etc., there would be great benefits in operations such as deoxidation.
鋼中の酸素を測定する方法としては、溶解炉中
あるいは取鍋中から溶鋼を汲取つて試料を調整し
分析する間接分析法と、固体電解質センサー等を
直接溶鋼に浸漬して其の熱起電力を測定する等の
直接分析法とがある。 There are two methods for measuring oxygen in steel: an indirect analysis method in which molten steel is drawn from a melting furnace or a ladle, the sample is prepared and analyzed, and a solid electrolyte sensor is directly immersed in the molten steel to detect its thermoelectromotive force. There are direct analysis methods such as measuring .
前者は最も一般的に普及し、古くからの化学的
方法であるハーテイー法から真空溶解法、不活性
ガス送気法を経て最近の放射化分析法へと各種の
方法が開発され、精度も高くまた分析所要時間も
最近では2分乃至1分と迅速性が向上し、製鋼分
野での管理分析法として広く定着するに至つてい
るが、これらの方法は分析そのものは迅速に行え
るようになつたが、何れも固体金属から試料をつ
くる必要があり、サンプリングを含めた分析試料
の調整に、時間、手数を要するため、分析結果を
作業現場へフイードバツクし、直ちに効果的な行
動がとれる迄には至つていない。 The former is the most common method, and various methods have been developed, from the old chemical method Hartey method to the vacuum dissolution method and inert gas blowing method, to the recent activation analysis method, and it is also highly accurate. In addition, the time required for analysis has recently improved from 2 minutes to 1 minute, and it has become widely established as a control analysis method in the steel manufacturing field, but the analysis itself can now be performed quickly. However, in both cases, it is necessary to prepare samples from solid metals, and preparation of analysis samples including sampling takes time and effort. I haven't reached it yet.
また後者の溶鋼中の酸素を直接分析する方法
は、作業現場へフイードバツクできる迅速性は好
ましいものであるが、固体電解質を用いて電気化
学的方法も、溶鋼が凝固する際に放出するガス量
より溶鋼中の酸素量を推定するガス圧測定法も未
だ試験段階であつて、操作性あるいは精度等に問
題が残され、またこれらの方法は何れも溶鋼中の
自由酸素量を測定するものであつて、鋼の内質を
評価する全酸素量の測定は前者間接分析法によら
ねばならないのが現状である。 The latter method, which directly analyzes oxygen in molten steel, is preferable because it allows for quick feedback to the work site, but electrochemical methods using solid electrolytes are also less effective than the amount of gas released when molten steel solidifies. The gas pressure measurement method for estimating the amount of oxygen in molten steel is still in the experimental stage, and there are still problems with operability and accuracy, and all of these methods measure the amount of free oxygen in molten steel. Therefore, the current situation is that the measurement of the total oxygen content for evaluating the internal quality of steel must be performed using the former indirect analysis method.
上記実状に鑑み、本発明の目的は溶鋼中に懸濁
している酸化物を含めた全酸素量を、直接法によ
り迅速に定量する、簡易且つ精度のよい方法を提
供するにある。 In view of the above circumstances, an object of the present invention is to provide a simple and accurate method for quickly quantifying the total amount of oxygen, including oxides, suspended in molten steel by a direct method.
前記した間接分析法は溶鋼を汲みとつて凝固さ
せ、この固体金属を高温のカーボン坩堝中で融解
し、炭素(C)を触媒とした還元反応C+O→
COにより生成した反応生成ガス(CO)を種々の
方法で計測定量するものであるが、本発明方法
は、このCO反応による方法を直接溶鋼で生ぜし
めるようにした点に特徴がある。 In the indirect analysis method described above, molten steel is pumped and solidified, this solid metal is melted in a high-temperature carbon crucible, and a reduction reaction C + O → using carbon (C) as a catalyst is performed.
The reaction product gas (CO) produced by CO can be measured and quantified using various methods, but the method of the present invention is characterized in that the CO reaction is directly produced in molten steel.
すなわち本発明は、炭素質物質を内装し不活性
ガス雰囲気とした耐火性プローベを金属溶湯中に
浸漬して前記炭素質物質と溶湯とを管内で接触さ
せ一酸化炭素を生成させる工程と、該生成ガスを
定量系に導いて一酸化炭素量を定量し、それより
酸素量を算出する工程とよりなる、溶鋼中酸素の
迅速分析法を要旨とする。 That is, the present invention includes a step of immersing a refractory probe with a carbonaceous material inside and an inert gas atmosphere in a molten metal to bring the carbonaceous material and the molten metal into contact in a pipe to generate carbon monoxide; The gist of this paper is a rapid analysis method for oxygen in molten steel, which consists of the steps of guiding the generated gas to a quantitative system, quantifying the amount of carbon monoxide, and then calculating the amount of oxygen.
反応媒体としての炭素質物質には、例えば繊維
状のカーボンが適当である。このカーボンを耐火
物カプセル等に充填し、プローベの不透明石英管
等に内装する。この反応管の先端には溶鋼を進入
させるための小孔が設けてあり、また管内へは予
め圧力、流量をコントロールしたArあるいはHe
等の不活性ガスを送給するようにし、管内を無酸
素状態に保つ。このための不活性ガスの圧力0.5
〜1.5Kg/cm2流量は1〜2/minである。カー
ボンを内装したプローベは機械力あるいは手動に
より直接測定しようとする溶鋼内に挿入する。溶
鋼が先端の小孔より管内に進入し、カーボンとの
接触によりCO反応が生じる。管内に送給される
不活性ガスは反応管内のCOガス分圧を下げCO反
応を促進させる。反応生成ガスは不活性ガスと共
にガスサンプリングポンプで吸引し、定量分析系
へ送られる。生成ガスの定量分析は例えば赤外線
吸収法等により行われる。 For example, fibrous carbon is suitable as the carbonaceous material as the reaction medium. This carbon is filled into a refractory capsule, etc., and placed inside the opaque quartz tube of the probe. A small hole is provided at the tip of this reaction tube to allow molten steel to enter, and Ar or Helium gas is introduced into the tube with pre-controlled pressure and flow rate.
The inside of the pipe is maintained in an oxygen-free condition by supplying an inert gas such as Inert gas pressure 0.5 for this
~1.5Kg/ cm2 flow rate is 1-2/min. A carbon-filled probe is inserted mechanically or manually into the molten steel to be directly measured. Molten steel enters the tube through the small hole at the tip, and a CO reaction occurs when it comes into contact with carbon. The inert gas fed into the tube reduces the partial pressure of CO gas inside the reaction tube and promotes the CO reaction. The reaction product gas is sucked together with an inert gas by a gas sampling pump and sent to a quantitative analysis system. Quantitative analysis of the generated gas is performed, for example, by infrared absorption method.
第1図は上記CO反応管を含むプローベの機構
図である。 FIG. 1 is a mechanical diagram of a probe including the above-mentioned CO reaction tube.
図において、1は反応管であつて、例えば不透
明石英管等でつくられ、小径管部2と小径管部に
続く大径管部3があり、端部の絞つた前記小径管
部の先端に溶鋼を内部に取り入れる小孔4を有し
ている。 In the figure, reference numeral 1 denotes a reaction tube, which is made of, for example, an opaque quartz tube, and has a small diameter tube section 2 and a large diameter tube section 3 following the small diameter tube section. It has a small hole 4 through which molten steel is introduced.
前記絞部はプローベを溶鋼中に浸漬する際の基
準線となると共に、続く大径管部へとCO反応時
に溶湯が飛散して小径管部を閉塞することのない
ように拡大されている。 The constricted portion serves as a reference line when the probe is immersed in molten steel, and is enlarged to prevent the molten metal from scattering into the subsequent large-diameter pipe portion during the CO reaction and block the small-diameter pipe portion.
5は耐熱性の例えばステンレス管でつくつた把
持部であつて、其の先端に前記反応管1の基部が
接続金具6a,6bにより着脱するよう設けられ
ている。すなわち、把持管部側に螺着する接続金
具6aのソケツト孔に反応管1の基部を挿入し、
周囲にOリング7を嵌め、リング状の接続金具6
bを前記金具6aに螺着し締め付けることによ
り、把持管5に反応管1が気密に接続固定され
る。 Reference numeral 5 denotes a gripper made of a heat-resistant stainless steel tube, for example, and the base of the reaction tube 1 is attached to and removed from the tip of the gripper by means of connecting fittings 6a and 6b. That is, insert the base of the reaction tube 1 into the socket hole of the connecting fitting 6a that is screwed onto the grip tube side,
Fit the O-ring 7 around the ring-shaped connection fitting 6
By screwing b into the metal fitting 6a and tightening it, the reaction tube 1 is connected and fixed to the grip tube 5 in an airtight manner.
8及び9は例えば内径4mm、外径6mmのス
テンレス管である。管8は反応管1の炭素質物質
をいれる小径管部2近く迄延在して開口し、この
管8より予め定量、定圧にコントロールされた不
活性ガスが反応管内に送り込まれる。 8 and 9 are stainless steel tubes with an inner diameter of 4 mm and an outer diameter of 6 mm, for example. The tube 8 extends and opens near the small diameter tube portion 2 of the reaction tube 1 into which the carbonaceous material is introduced, and an inert gas whose constant pressure is controlled in advance is fed into the reaction tube through the tube 8.
管9はプローベが溶鋼中に挿入され溶鋼が反応
管1の小径管部2内に進入し、炭素質物質と接触
して生成する一酸化炭素を前記管8から送入され
る不活性ガスと共に反応管外のサンプリング系へ
とり出すためのサンプリングガス搬送管で反応管
1の基部付近に開口する。 In the tube 9, a probe is inserted into the molten steel, and the molten steel enters the small diameter tube section 2 of the reaction tube 1, and carbon monoxide generated when it comes into contact with carbonaceous material is collected together with the inert gas sent from the tube 8. A sampling gas transport pipe for taking out to a sampling system outside the reaction tube opens near the base of the reaction tube 1.
第2図は、前記プローベへ定量、定圧の不活性
ガスを送出する不活性ガス送給系Aと、プローベ
内で生成された一酸化炭素を送り込んだ不活性ガ
スと共にとり出すガスサンプリング系B、及びサ
ンプリングしたガスの一酸化炭素量を定量し、鋼
中酸素量を表示する定量系Cの一例を示すフロー
チヤートである。 FIG. 2 shows an inert gas supply system A that sends a fixed amount of inert gas at a constant pressure to the probe, a gas sampling system B that takes out carbon monoxide generated in the probe together with the inert gas sent, It is a flowchart showing an example of quantitative system C that quantitatively determines the amount of carbon monoxide in the sampled gas and displays the amount of oxygen in the steel.
不活性ガス送給系Aは、圧力計P1,P2、調圧
弁C1、流量調整弁C2を備え、Ar又はHeポンベか
らの不活性ガスを定量、定圧に調整し、フイルタ
ーf1、脱水剤Hを通し、流量計F1を経てプローベ
の前記管8より不活性ガスを送出する。 The inert gas supply system A is equipped with pressure gauges P 1 , P 2 , a pressure regulating valve C 1 , and a flow rate regulating valve C 2 , and adjusts the inert gas from the Ar or He pump to a fixed amount and constant pressure . , a dehydrating agent H, and an inert gas is sent out from the tube 8 of the probe via a flowmeter F1 .
またガスサンプリングガス系Bは、サンプリン
グポンプを備えプローベ内での反応生成ガスを定
量系Cへ搬送するサンプリングユニツトS、サン
プリングガスを過するフイルターf2、サンプリ
ングユニツトで分離された湿分を受けるドレンポ
ツトd、その排液コツクC4よりなる。 The gas sampling gas system B includes a sampling unit S that is equipped with a sampling pump and conveys the reaction product gas in the probe to the quantitative system C, a filter f 2 that passes the sampling gas, and a drain pot that receives the moisture separated by the sampling unit. d. Consists of its drainage pot C 4 .
定量系Cは、サンプリングガス中のCO量を定
量するため例えば赤外線吸収法によるCOメータ
ーM、その測定値をモニターして記録する記録計
K、COメーターMで得られたガスピーク値を積
分する積分器I及びその数値を印字する表示器P
等を備え、前記サンプリングユニツトSから搬送
されるサンプリングガスは三方弁C5により流量
計F2を経てCOメーターMに送られる。送られた
生成COガスはCOメーターMで定量され記録紙上
にピークとして記録され、同時に積分器Iにより
面積積分され数値として表示部Pにデジタル印字
される。なおB1,B2はCOメーターMの校正用の
標準ガスである。 The quantitative system C includes a CO meter M using an infrared absorption method to quantify the amount of CO in the sampling gas, a recorder K that monitors and records the measured value, and an integral that integrates the gas peak value obtained by the CO meter M. Display unit I and display unit P that prints its numerical value
The sampling gas conveyed from the sampling unit S is sent to the CO meter M via a flowmeter F2 by a three-way valve C5 . The generated CO gas sent is quantified by a CO meter M and recorded as a peak on a recording paper, and at the same time is integrated by area by an integrator I and digitally printed as a numerical value on a display section P. Note that B 1 and B 2 are standard gases for calibrating the CO meter M.
本発明の直接溶鋼中酸素の分析法が有効である
ためには、本法の溶鋼酸素値と固体資料のガス分
析値との間に相関のあることが示されなければな
らないが、両者の関係を表わしたのが第3図であ
る。 In order for the method of directly analyzing oxygen in molten steel of the present invention to be effective, it must be shown that there is a correlation between the molten steel oxygen value of this method and the gas analysis value of the solid material. Figure 3 shows this.
この測定例は1トン高周波炉で大気溶解した
Fe−Ni合金の酸素ガス量を本法で測定すると共
に同時に汲取つた固体資料から酸素を分析した数
値も併せて示したものである。本発明方法はCO
ガスのピーク面積の積分値を溶鋼反応量1g当り
のO2量に換算した数値であり(横軸)、固体資料
の数値は不活性ガス分析法による固体金属中の全
酸素量をppmで示したものである(縦軸)。炉前
での反応量の誤差も含めて両方法間には多少のバ
ラツキはあるが略々良好な相関関係を示し、本法
が実用上十分な精度を有することを示している。 In this measurement example, atmospheric melting was performed in a 1-ton high-frequency furnace.
The amount of oxygen gas in the Fe-Ni alloy was measured using this method, and the values obtained by analyzing the oxygen from the solid material collected at the same time are also shown. The method of the present invention
This is the value obtained by converting the integrated value of the gas peak area into the amount of O 2 per gram of molten steel reaction amount (horizontal axis), and the value of the solid data shows the total amount of oxygen in the solid metal in ppm according to the inert gas analysis method. (vertical axis). Although there are some variations between the two methods, including errors in the amount of reaction before the furnace, they show a generally good correlation, indicating that the present method has sufficient accuracy for practical use.
従来の間接法に依るときはサンプリングから結
果が判明する迄に約30分と時間がかゝりすぎ現場
操業に結果を直ちにフイードバツクすることは到
底下可能であつたが、本発明は溶鋼中の酸素量挙
動が炉前で迅速に把握でき、従つて例えば、出鋼
時の脱酸剤投入量の調整も有効に実施できる等の
効果がある。 When relying on the conventional indirect method, it took about 30 minutes from sampling to obtain the results, which was too long, making it impossible to immediately feed back the results to on-site operations, but the present invention The oxygen content behavior can be quickly grasped in front of the furnace, and therefore, for example, the amount of deoxidizing agent input during tapping can be effectively adjusted.
第1図は本法の実施に適した溶鋼中に挿入する
プローベの機構説明図、第2図はプローベへ定
量、定圧の不活性ガスを送出する不活性ガス送給
系A、プローベ内での生成ガスサンプリング系B
及びサンプリングしたガスの一酸化炭素ガスの定
量系Cの一例を示すフローチヤート。第3図は本
法による溶鋼中の酸素値と従来の不活性ガス送気
法によるガス分析値とを対比した図表である。
1:反応管、2:小径管部、3:大径管部、
4:小孔、5:把持部、6:接続金具、7:Oリ
ング、8:不活性ガス送給管、9:サンプリング
ガス搬送管、A:不活性ガス送給系、B:ガスサ
ンプリング系、C:一酸化炭素ガス定量系、P1,
P2:圧力計、C1:調圧弁、C2:流量調整弁、f1,
f2:フイルター、Hs:脱水剤、F1,F2:流量計、
S:サンプリングユニツト、d:ドレンポツト、
M:COメーター、K:記録計、I:積分器、
P:表示器、C3,C4:コツク、C5:三方コツク、
B1,B2:標準ガス。
Figure 1 is an explanatory diagram of the mechanism of a probe inserted into molten steel suitable for implementing this method. Figure 2 is an inert gas supply system A that delivers a fixed amount of inert gas to the probe at a constant pressure. Produced gas sampling system B
and a flowchart showing an example of a system C for quantifying carbon monoxide gas in a sampled gas. FIG. 3 is a chart comparing the oxygen value in molten steel obtained by this method with the gas analysis value obtained by the conventional inert gas blowing method. 1: reaction tube, 2: small diameter tube section, 3: large diameter tube section,
4: Small hole, 5: Grip, 6: Connection fitting, 7: O-ring, 8: Inert gas supply pipe, 9: Sampling gas transport pipe, A: Inert gas supply system, B: Gas sampling system , C: Carbon monoxide gas quantitative system, P 1 ,
P 2 : Pressure gauge, C 1 : Pressure regulating valve, C 2 : Flow regulating valve, f 1 ,
f 2 : Filter, Hs : Dehydrating agent, F 1 , F 2 : Flow meter,
S: Sampling unit, d: Drain pot,
M: CO meter, K: recorder, I: integrator,
P: Display, C 3 , C 4 : Kotoku, C 5 : Three-way Kotoku,
B 1 , B 2 : Standard gas.
Claims (1)
耐火性プローベを金属溶湯中に浸漬して炭素質物
質と溶湯とを管内で接触させ一酸化炭素を生成さ
せる工程と、該生成ガスを定量系に導いて一酸化
炭素量を定量し、それより酸素量を算出する工程
とよりなることを特徴とする溶鋼中酸素の迅速分
析方法。 2 先端に小孔のある小径管部と小径管部に続く
大径管部よりなる反応管をその基部において接続
金具で把持部に着脱するよう設けて前記小径管部
内に炭素質物質を収容するとともに、前記反応管
内の小径管部近くに開口して反応管内に定量、定
圧の不活性ガスを送給する不活性ガス送給管と、
反応管内に開口して発生ガスをガスサンプリング
系に運び出すサンプリングガス取出管とを、反応
管内と気密に連絡するよう取付けてなるプローベ
を備えたことを特徴とする溶鋼中酸素の迅速分析
装置。[Claims] 1. A step of immersing a fire-resistant probe with a carbonaceous material inside and an inert gas atmosphere into molten metal to bring the carbonaceous material and molten metal into contact in the pipe to generate carbon monoxide; 1. A method for rapid analysis of oxygen in molten steel, comprising the steps of guiding the generated gas to a quantitative system, quantifying the amount of carbon monoxide, and calculating the amount of oxygen therefrom. 2. A reaction tube consisting of a small diameter tube section with a small hole at the tip and a large diameter tube section following the small diameter tube section is provided at its base so that it can be attached to and detached from the grip section using a connecting fitting, and the carbonaceous material is housed in the small diameter tube section. and an inert gas feed pipe that opens near the small diameter pipe portion of the reaction tube and feeds a fixed amount of inert gas at a constant pressure into the reaction tube;
A rapid analysis device for oxygen in molten steel, characterized in that the probe is equipped with a sampling gas take-off tube that opens into the reaction tube and carries generated gas to a gas sampling system, and is installed in airtight communication with the inside of the reaction tube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8307280A JPS578450A (en) | 1980-06-18 | 1980-06-18 | Method and apparatus for rapid analysis of oxygen in molten steel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8307280A JPS578450A (en) | 1980-06-18 | 1980-06-18 | Method and apparatus for rapid analysis of oxygen in molten steel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS578450A JPS578450A (en) | 1982-01-16 |
| JPS6321864B2 true JPS6321864B2 (en) | 1988-05-09 |
Family
ID=13791967
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8307280A Granted JPS578450A (en) | 1980-06-18 | 1980-06-18 | Method and apparatus for rapid analysis of oxygen in molten steel |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS578450A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| 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 |
-
1980
- 1980-06-18 JP JP8307280A patent/JPS578450A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS578450A (en) | 1982-01-16 |
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