JPS6011085B2 - Decarburization measurement device in vacuum decarburization furnace - Google Patents
Decarburization measurement device in vacuum decarburization furnaceInfo
- Publication number
- JPS6011085B2 JPS6011085B2 JP10521577A JP10521577A JPS6011085B2 JP S6011085 B2 JPS6011085 B2 JP S6011085B2 JP 10521577 A JP10521577 A JP 10521577A JP 10521577 A JP10521577 A JP 10521577A JP S6011085 B2 JPS6011085 B2 JP S6011085B2
- Authority
- JP
- Japan
- Prior art keywords
- decarburization
- vacuum
- gas
- furnace
- mass spectrometer
- 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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
- C21C7/10—Handling in a vacuum
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Other Investigation Or Analysis Of Materials By Electrical Means (AREA)
- Investigating, Analyzing Materials By Fluorescence Or Luminescence (AREA)
- Sampling And Sample Adjustment (AREA)
Description
【発明の詳細な説明】
この発明は真空脱蕨炉による真空精錬過程において、排
出されるガスを質量分析計によって分析し排出ガス特に
炭素排出量を測定する装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for measuring exhaust gas, particularly carbon emissions, by analyzing exhaust gas using a mass spectrometer during a vacuum refining process using a vacuum descaling furnace.
一般に鋼中の炭素はその鋼の品質および機械的性質に重
要な役割を果すため製鋼工程特に最終精錬工程において
終点炭素値を製品目標炭素値に合致させることは重要な
課題である。In general, carbon in steel plays an important role in the quality and mechanical properties of the steel, so it is an important issue to match the end point carbon value to the product target carbon value in the steelmaking process, especially in the final refining process.
そのため最近この終点炭素値を制御するために数多〈の
研究が行なわれており特に転炉においてはその研究がさ
かんであり排ガス量および排ガス組成等をモデル化した
ダイナミック制御方法等が行なわれている。Therefore, a lot of research has recently been conducted to control this end point carbon value, and this research is particularly active in converters, and dynamic control methods that model the exhaust gas amount and exhaust gas composition, etc. are being carried out. There is.
一方ステンレス鋼の製造過程においては、クロムの酸化
による損失を減少させるために真空(減圧)を利用して
脱炭を行なう方法が実施されている。On the other hand, in the process of manufacturing stainless steel, a method of decarburizing using vacuum (reduced pressure) is used to reduce the loss of chromium due to oxidation.
この方法において終点炭素値を安定させることは単にC
r歩蟹を向上させるということだけでなく溶鋼中の酸素
濃度を下げかつそのバラッキを減少し清浄な鍵を製造す
るという意味でも重要である。ところで、この考案にか
)わる真空脱炭炉における終点炭素値の制御方法につい
ては転炉の場合ほど充分に研究は行なわれておらずその
ための脱炭量測定には種々の欠点を有している。すなわ
ち従来ではベンチュリー管などにより排気ガスの絶対量
を求めるようにしているが、この場合は応答特性に問題
があり精度も十分でない。又真空機器からのりークもあ
りしかもそのリークが温度により変化してリーク量を検
知することは困難である。また真空精錬途中の変動要因
による誤差を制御することは困難な状況にある。このよ
うな事情から従来においては脱炭量測定が精度良好に行
なわれず終点炭素制御が良好に行なわれていないのが実
情である。このような状況にかんがみて質量分析計方式
のガス分析器を利用しトレーサガスを加えてこれを測定
媒体とし測定ガスおよびこのトレーサガス分圧値などか
ら排出ガス量を測定する画期的な方法(特関昭50−9
9592号「ガス発生室におけるガス発生量の測定方法
および装置しが提案されている。In this method, stabilizing the end point carbon value is simply C
This method is important not only for improving the quality of the steel, but also for lowering the oxygen concentration in the molten steel and reducing its dispersion, thereby producing clean keys. By the way, the method of controlling the end point carbon value in a vacuum decarburization furnace according to this invention has not been studied as thoroughly as in the case of a converter, and there are various drawbacks in measuring the amount of decarburization. There is. That is, conventionally, the absolute amount of exhaust gas is determined using a venturi tube or the like, but in this case, there are problems with the response characteristics and the accuracy is not sufficient. There is also leakage from the vacuum equipment, and the leakage changes depending on the temperature, making it difficult to detect the amount of leakage. Furthermore, it is difficult to control errors caused by fluctuation factors during vacuum refining. Due to these circumstances, the actual situation is that in the past, the amount of decarburization has not been measured with good accuracy and end point carbon control has not been performed well. In view of this situation, we have developed an innovative method that uses a mass spectrometer type gas analyzer to add a tracer gas and uses this as a measurement medium to measure the amount of exhaust gas from the measurement gas and the partial pressure value of this tracer gas. (Tokusei Showa 50-9
No. 9592 proposes a method and apparatus for measuring the amount of gas generated in a gas generation chamber.
この考案はこの新しい方法を真空脱炭炉において精度よ
く実施できる脱炭量測定装置を提供しようとするもので
ある。すなわちこの発明は測定すべき炭素ガスおよびト
レーサガスをガス分析器に採取する採取路にコンダクタ
ンスを可変できるバルブ機構を介設しこのバルブ機構の
作動によってガス分析器(質量分析計)内の圧力を常に
最適状態にするようにした脱炭量測定装置である。This invention aims to provide a decarburization amount measuring device that can accurately implement this new method in a vacuum decarburization furnace. That is, this invention provides a valve mechanism that can vary the conductance in a sampling path through which carbon gas and tracer gas to be measured are sampled into a gas analyzer, and the pressure inside the gas analyzer (mass spectrometer) is controlled by the operation of this valve mechanism. This is a decarburization amount measuring device that is always in the optimum state.
以下図面に示される実施例にしたがってこの発明を説明
する。第1図はこの発明による測定装置の概略図であり
第2図は要部拡大図、第3図は変形実施例を示す図であ
る。The present invention will be described below according to embodiments shown in the drawings. FIG. 1 is a schematic diagram of a measuring device according to the present invention, FIG. 2 is an enlarged view of the main part, and FIG. 3 is a diagram showing a modified embodiment.
1は真空脱蕨炉で溶鋼3の入った取鍋2が内側に置かれ
ている。1 is a vacuum descaling furnace, and a ladle 2 containing molten steel 3 is placed inside.
この真空脱炭炉1は排気ダクト5を介してェジェクター
6により排気される。7はコンデンサーである。This vacuum decarburization furnace 1 is exhausted by an ejector 6 via an exhaust duct 5. 7 is a capacitor.
この排気によって炉1内が所定の真空度に達すると、ラ
ンスパィプ4によって気体酸素を吹精するが、このとき
気体酸素吹糟前および吹糟中において溶鋼中の炭、素の
一部は鋼中溶存酸素または気体酸素と反応しすべてCO
またはC02ガスとなり排気ダクト5により排気される
。8は排気ダクト5にガス採取管10を接続した位置を
示し、16は排気ダクト5にトレーサガスを供給する位
置を示している。When the inside of the furnace 1 reaches a predetermined degree of vacuum due to this evacuation, gaseous oxygen is blown out by the lance pipe 4, but at this time, before and during the blowing of the gaseous oxygen, some of the carbon and elements in the molten steel are removed from the steel. Reacts with dissolved or gaseous oxygen to produce all CO
Alternatively, it becomes C02 gas and is exhausted through the exhaust duct 5. 8 indicates the position where the gas sampling pipe 10 is connected to the exhaust duct 5, and 16 indicates the position where the tracer gas is supplied to the exhaust duct 5.
9はトレーサガスすなわちアルゴンガスなどの不活性ガ
スのボンベである。9 is a cylinder for tracer gas, that is, an inert gas such as argon gas.
採取管10の終端はガス分析を行なう質量分析計15に
接続されており、11はこの管路に介設されたダストト
ラツプである。12はこの発明の特徴とする可変コンダ
クタンスバルブで採取管略10に介在されており排気ダ
クト5に設置された真空計18からの信号によりそのコ
ンダクタンスの調整が行なわれるようになっている。The terminal end of the collection tube 10 is connected to a mass spectrometer 15 for gas analysis, and 11 is a dust trap interposed in this tube. Reference numeral 12 denotes a variable conductance valve, which is a feature of the present invention, and is interposed in the sampling pipe 10, and its conductance is adjusted by a signal from a vacuum gauge 18 installed in the exhaust duct 5.
10′はコンデンサ−7からの排気ガスをバルブ19お
よび採取管10を介して質量分析計15に導入する採取
管である。Reference numeral 10' denotes a sampling tube for introducing exhaust gas from the condenser 7 into the mass spectrometer 15 via a valve 19 and a sampling tube 10.
13は排気ダクト5から採取されたガスを質量分析計1
5に導入するための真空ポンプであり14は質量分析計
排気ポンプである。13 is a mass spectrometer 1 for the gas sampled from the exhaust duct 5.
5 is a vacuum pump for introducing the mass spectrometer, and 14 is a mass spectrometer exhaust pump.
また17はトレーサガスを供V給するためのバルブであ
りトレーサガスを排気ダクト5に供給するに際して操作
され連続的供給あるいは間歌的供給が行なわれる。以上
のような構成であるから排気ダクト5にトレーサガスが
供給されるとそのガスは炉1からのガスに混入され均一
に分布されて排気されることになる。Reference numeral 17 denotes a valve for supplying the tracer gas, which is operated when supplying the tracer gas to the exhaust duct 5 to perform continuous supply or intermittent supply. With the above configuration, when the tracer gas is supplied to the exhaust duct 5, the gas is mixed with the gas from the furnace 1, and is uniformly distributed and exhausted.
そして採取管10を介して試料ガス(排気ガスとトレー
サガス)が採取される(あるいは採取管10′から採取
される)が、この時一連の採取系はその圧力が大気圧(
760Torr)から0.1Tor「&まで変化する。
したがって従来の場合このような圧力変化が起こると質
量分析計15に導入される試料ガス量が変動することに
なる。しかし質量分析計15の分析圧力の最適条件は1
0‐5〜10‐的orrでありしたがって上記のような
変動は分析精度を低下させるのみでなく分析計内の圧力
上昇を招いて分析管の加熱フィラメントの劣化をまねく
ことになるのである。この発明はこのような従釆の問題
点を完全に解消するものである。Sample gases (exhaust gas and tracer gas) are then sampled through the sampling tube 10 (or sampled from the sampling tube 10');
It varies from 760 Torr) to 0.1 Torr.
Therefore, in the conventional case, when such a pressure change occurs, the amount of sample gas introduced into the mass spectrometer 15 changes. However, the optimal condition for the analysis pressure of the mass spectrometer 15 is 1
0-5 to 10-orr, and therefore, the above-mentioned fluctuation not only lowers the accuracy of analysis, but also causes a rise in pressure within the analyzer, leading to deterioration of the heating filament of the analysis tube. The present invention completely solves the problems of this conventional method.
すなわち、試料ガスの質量分析計15への導入部の圧力
変化に応じて試料ガスの質量分析計への導入を調節する
ようにしたものであって第2図にも示すとおりこの調節
を可変コンダクタンスバルブ12によって行なわせるよ
うにしたものである。このバルブ12は排気ダクト5の
圧力によって調節される。したがって圧力の変化に対し
ても常にほジー一定量の試料ガスを質量分析計15に導
入することができる。第3図はこの発明の変形実施例で
あって1個のバルブ12のコンダクタンスを調節する方
式ではなく、それぞれコンダクタンスの異なる複数個の
バルブ12一1〜12−3を並列的に採取路10に介設
し、これらの作動開始制御を真空計18からの信号によ
り行なわせる実施例である。That is, the introduction of the sample gas into the mass spectrometer is adjusted according to the pressure change at the introduction part of the sample gas into the mass spectrometer 15, and as shown in FIG. This is done by the valve 12. This valve 12 is regulated by the pressure in the exhaust duct 5. Therefore, a constant amount of sample gas can always be introduced into the mass spectrometer 15 even when the pressure changes. FIG. 3 shows a modified embodiment of the present invention in which the conductance of one valve 12 is not adjusted, but a plurality of valves 12-1 to 12-3 each having a different conductance are connected to the sampling path 10 in parallel. In this embodiment, a vacuum gauge 18 is provided to control the start of these operations using a signal from a vacuum gauge 18.
このようにコンダクタンスを可変できるバルブ機構につ
いては種々の変形実施例を挙げることができよう。その
他排気系、採取系についても図示例以外種々の変形実施
例を挙げることができよう。この発明は以上説明したと
おりであるから、質量分析計が精度よく試料ガスの分析
を行なうことを保障し、したがって特に排気ガスすなわ
ち炭素の排気量測定を精度良好に測定できるので脱炭炉
としてすぐれた脱炭量測定装置を提供するものである。
バルブ機構のコンダクタンス可変範囲を調整することに
よって質量分析計として最適の分析条件を得ることがで
き分析精度終局的には測定精度を向上させることができ
る。As for the valve mechanism that can vary the conductance in this way, various modified embodiments can be mentioned. Various other modified embodiments other than those shown in the drawings may be made regarding the exhaust system and sampling system. As explained above, the present invention ensures that the mass spectrometer analyzes the sample gas with high precision, and therefore can measure the amount of exhaust gas, that is, carbon, with high precision, making it an excellent decarburization furnace. The present invention provides a device for measuring the amount of decarburization.
By adjusting the conductance variable range of the valve mechanism, the optimum analysis conditions for the mass spectrometer can be obtained, and the analysis accuracy and ultimately the measurement accuracy can be improved.
第1図はこの発明による測定装置の概略図、第2図は要
部拡大図、第3図は変形実施例を示す図である。
1・・・…真空脱炭炉、5・・・・・・排気ダクト、7
・・・・・・コンデンサー、10,10′・・・・・・
採取管、12・・・・・・可変コンダクタンスバルブ、
13・・・・・・真空ポンプ、15・・・・・・質量分
析計、18・・・…真空計。
オ1図す2図
才3図FIG. 1 is a schematic diagram of a measuring device according to the present invention, FIG. 2 is an enlarged view of the main part, and FIG. 3 is a diagram showing a modified embodiment. 1...Vacuum decarburization furnace, 5...Exhaust duct, 7
...... Capacitor, 10,10'...
Collection tube, 12...variable conductance valve,
13... Vacuum pump, 15... Mass spectrometer, 18... Vacuum gauge. 1 diagram, 2 diagrams, 3 diagrams
Claims (1)
炭素、二酸化炭素とトレーサガスを質量分析計によって
分析し、この各ガスの分圧とトレーサガス供給量から脱
炭量を測定するようにした装置において、前記真空脱炭
炉の排気ダクトから前記各ガスを質量分析計に採取する
採取路にそのコンダクタンスを可変できるバルブ機構を
設置し、前記真空脱炭炉を減圧する過程で順次コンダク
タンスを大ならしめるようバルブ機構を作動させ質量分
析側の採取ガス圧力の変化を小さくしたことを特徴とす
る真空脱炭炉における脱炭量測定装置。1 The carbon monoxide, carbon dioxide, and tracer gas emitted during the vacuum refining process using the vacuum decarburization furnace are analyzed using a mass spectrometer, and the amount of decarburization is measured from the partial pressure of each gas and the amount of tracer gas supplied. In this apparatus, a valve mechanism capable of varying the conductance is installed in the sampling path through which each of the gases is sampled from the exhaust duct of the vacuum decarburization furnace to a mass spectrometer, and the conductance is sequentially adjusted in the process of depressurizing the vacuum decarburization furnace. 1. A decarburization amount measuring device in a vacuum decarburization furnace, characterized in that a valve mechanism is operated to reduce changes in sampled gas pressure on the mass spectrometry side to increase decarburization.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10521577A JPS6011085B2 (en) | 1977-08-31 | 1977-08-31 | Decarburization measurement device in vacuum decarburization furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10521577A JPS6011085B2 (en) | 1977-08-31 | 1977-08-31 | Decarburization measurement device in vacuum decarburization furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5438212A JPS5438212A (en) | 1979-03-22 |
| JPS6011085B2 true JPS6011085B2 (en) | 1985-03-23 |
Family
ID=14401438
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10521577A Expired JPS6011085B2 (en) | 1977-08-31 | 1977-08-31 | Decarburization measurement device in vacuum decarburization furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6011085B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61215980A (en) * | 1985-03-20 | 1986-09-25 | Nec Corp | Synthetic aperture radar device |
| JPS63238482A (en) * | 1987-03-26 | 1988-10-04 | Japan Radio Co Ltd | Mls receiver |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0413668U (en) * | 1990-05-18 | 1992-02-04 |
-
1977
- 1977-08-31 JP JP10521577A patent/JPS6011085B2/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61215980A (en) * | 1985-03-20 | 1986-09-25 | Nec Corp | Synthetic aperture radar device |
| JPS63238482A (en) * | 1987-03-26 | 1988-10-04 | Japan Radio Co Ltd | Mls receiver |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5438212A (en) | 1979-03-22 |
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