JPH02156012A - Method for reducing dust in exhaust gas in converter blowing - Google Patents

Method for reducing dust in exhaust gas in converter blowing

Info

Publication number
JPH02156012A
JPH02156012A JP30992388A JP30992388A JPH02156012A JP H02156012 A JPH02156012 A JP H02156012A JP 30992388 A JP30992388 A JP 30992388A JP 30992388 A JP30992388 A JP 30992388A JP H02156012 A JPH02156012 A JP H02156012A
Authority
JP
Japan
Prior art keywords
dust
exhaust gas
blowing
gas
generating
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.)
Pending
Application number
JP30992388A
Other languages
Japanese (ja)
Inventor
Yoshihide Kato
嘉英 加藤
Yasuo Kishimoto
康夫 岸本
Toshikazu Sakuratani
桜谷 敏和
Tetsuya Fujii
徹也 藤井
Mutsumi Tada
睦 多田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP30992388A priority Critical patent/JPH02156012A/en
Publication of JPH02156012A publication Critical patent/JPH02156012A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To suitably restrain generating rate of dust in exhaust gas by continuously measuring the generating rate of the dust in the exhaust gas, rising the lance height when the generating speed of the dust becomes more than the setting upper limit value and mixing inert gas into top blowing gas. CONSTITUTION:In the blowing with a combined blowing converter 1, the flow rate of the exhaust gas is measured at downstream of a flue 5. On the way of the flue 5, the exhaust gas and the dust are sucked with a suction pipe 6 and introduced to a dust concn. meter 7 to measure the generating rate of the dust. From the values of this dust concn. and the exhaust gas flow rate, the generating speed of the dust is continuously displayed to the dust generating rate detector and controller 9. At the time of exceeding the setting value of the generating speed of the dust or the setting pattern, the height of the lance top-blowing the oxygen is risen. At the same time, the inert gas is mixed into the top blown oxygen gas. By this method, the generating ratio of the dust in the exhaust gas is reduced and the yield of the steelmaking is improved.

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は転炉吹錬における排ガス中のダスト低減方法に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION <Industrial Application Field> The present invention relates to a method for reducing dust in exhaust gas in converter blowing.

〈従来の技術〉 転炉精錬中に発生ずる排ガス中のダストは溶鉄中の金属
成分が蒸発したヒエ−ムダストと上吹きもしくは底吹き
などの方法で酸素ガスを鋼浴へ供給することによって生
じるバブルバースト系ダストに大別される。
<Prior art> Dust in the exhaust gas generated during converter refining is composed of Hiem dust, which is the evaporation of metal components in molten iron, and bubbles generated by supplying oxygen gas to the steel bath using methods such as top blowing or bottom blowing. It is broadly classified into burst type dust.

転炉精錬中に発生ずる排ガス中のダストを抑制するため
、上吹きランスの高さを下げる方法や上吹きランスの孔
径を拡大する方法などが周知である。しかし、これらの
方法ではダスト発生債を待ち時間なしに検出することが
不可能なので、ダスト抑制のためのタイムリーで適切な
制御手段とはなりえない、また、ランス高さや上吹きラ
ンスの孔径は他の冶金操業要因にも影響を与えるので、
ダスト抑制を常に最優先で合るとは限らない。
In order to suppress dust in the exhaust gas generated during converter refining, methods such as lowering the height of the top blowing lance and enlarging the hole diameter of the top blowing lance are well known. However, these methods cannot detect dust generation without waiting time, so they cannot be a timely and appropriate control measure for dust suppression. also affects other metallurgical operating factors, so
Dust suppression may not always be the top priority.

更に、特開昭60−262912号公報ではダスト兄1
からのダスト発生速度の情報に応じてランス高さを変更
するか、水蒸気をランスから吹付ける方法が開示されて
いる。しかし、適正なランス高さはダスト量のみによっ
て定まるのではなく前述したように池の冶金要因も絡む
、さらに水蒸気の吹付けは鋼中水素濃度を著しく高め、
脱水素のための追加アクシロンを講じる必要がでてくる
。ずなわら脱炭酸素効率を低下させたり、鋼中に不純物
成分が入るような操業は避りなk)ればならない。
Furthermore, in Japanese Patent Application Laid-Open No. 60-262912, Dust Brother 1
A method is disclosed in which the lance height is changed according to information on the dust generation rate from the lance, or water vapor is sprayed from the lance. However, the appropriate lance height is determined not only by the amount of dust, but also by the metallurgical factors of the pond, as mentioned above.In addition, spraying water vapor significantly increases the hydrogen concentration in the steel.
It becomes necessary to provide additional axilons for dehydrogenation. It is necessary to avoid operations that reduce decarburization oxygen efficiency or introduce impurity components into the steel.

〈発明が解決しようとする課題〉 転炉吹錬では同一送酸パターン、ランス高さの条件でも
溶鉄成分や温度、副原料投入時期を変えれば異なる吹錬
挙動を示す、したがってダスト発生量も各吹錬毎に異な
っており、悪条件が重なれば、前述した従来技術を用い
てもさほどの効果がない場合もしばしば存在する。
<Problem to be solved by the invention> In converter blowing, even if the oxygen supply pattern and lance height are the same, if the molten iron composition, temperature, and timing of adding auxiliary materials are changed, the blowing behavior will be different. Therefore, the amount of dust generated will also vary. Each blowing process is different, and under unfavorable conditions, there are often cases in which the above-mentioned conventional techniques are not very effective.

本発明は前述従来技術の問題点を解消し、転炉吹錬時に
発生ずる排ガス中のダストIをほぼリアルタイムで検出
することによってタイムリーかつ適切に排ガス中のダス
ト発生量を抑制すると共に冶金特性を改善することがで
き、更に吹錬の非再現性に対しても十分対応可能な転炉
吹錬における排ガス中のダスト低減方法を提供すること
を目的とするものである。
The present invention solves the problems of the prior art described above, detects dust I in the exhaust gas generated during converter blowing in almost real time, and thereby suppresses the amount of dust generated in the exhaust gas in a timely and appropriate manner. It is an object of the present invention to provide a method for reducing dust in exhaust gas in converter blowing, which can improve the process and also sufficiently deal with non-reproducibility of blowing.

く課題を解決するための手段〉 上記目的を達成するための本発明の転炉吹錬における排
ガス中のダスト低減方法は、転炉吹錬において、排ガス
中のダスト発生速度を連続的に計測し、その計測値がダ
スト発生速度の設定上限値を超えたときに酸素ガスを上
吹きするためのランスの高さを上昇すると同時に当該ラ
ンスから上吹きする酸素ガスに不活性ガスを混合させて
吹錬することを特徴とするものである。
Means for Solving the Problems> The method for reducing dust in exhaust gas in converter blowing of the present invention to achieve the above object continuously measures the rate of dust generation in exhaust gas in converter blowing. , when the measured value exceeds the upper limit set for the dust generation rate, the height of the lance for upward blowing of oxygen gas is raised, and at the same time, an inert gas is mixed with the oxygen gas blowing upward from the lance. It is characterized by training.

前述のように本発明を遂行するためには、i)吹錬中の
ダスト泣をリアルタイムで計測し。
As mentioned above, in order to carry out the present invention, it is necessary to: i) measure the dust flow during blowing in real time;

ii)任意に設定したダスト景上限値を超えたかどうか
を判断し。
ii) Determine whether an arbitrarily set dust scene upper limit value has been exceeded.

iii )過剰ダス1−fitとなった場合に抑制方策
をとる。
iii) Take control measures when excess das1-fit occurs.

ことが必要である。さらに、過剰ダスト量となった場合
にとるべき抑制対策として、 i)上吹きランス高さを上昇する。
It is necessary. Furthermore, the measures to be taken in case of excessive dust amount are: i) Raise the height of the top blowing lance.

it )上吹きランスから鋼浴へ吹付ける0、中にN!
it) 0 from the top blowing lance to the steel bath, N inside!
.

^「またはCOl等の不活性ガスを混合させる。^ ``Or mix in an inert gas such as COl.

本発明にはダスト発生量を連続して計測する装置(以下
、ダスト計と称する)が必要である。排ガス中のダスト
の採取は転炉排ガス煙道途中でも、また炉内で行っても
よい、ダスト採取のためのプローブは水冷または空冷と
し、ダスト計にダストが導入されるまでプローブ内にダ
ストが蓄積されない構造とする。
The present invention requires a device (hereinafter referred to as a dust meter) that continuously measures the amount of dust generated. The dust in the flue gas may be collected in the converter flue gas flue or inside the furnace.The probe for dust collection is water-cooled or air-cooled, and the dust is kept in the probe until it is introduced into the dust meter. The structure should be such that it does not accumulate.

ダスト計にはサンプルガスを吸引し、サンプルガスを光
学的に測定する光透過式または散乱式の測定器、超音波
による測定器、放射線による測定器等の種々のものがあ
るが、いずれを用いる場合にもダストが同伴される排ガ
ス流量と排ガス中のダスト濃度を知ればダスト発生量を
知ることができる。
There are various types of dust meters, such as light transmission type or scattering type measuring devices that aspirate sample gas and measure the sample gas optically, measuring devices using ultrasonic waves, and measuring devices using radiation, which one should you use? Even in such cases, the amount of dust generated can be determined by knowing the flow rate of the exhaust gas entrained with dust and the dust concentration in the exhaust gas.

このようにして転炉吹錬中にダスト発生量を連続して計
測し、任意の設定値以上となった時に抑制策をとる。抑
制策としては種々存在するがその中で以下の2方策を同
時に行った場合に最も敏感に応答することができる。
In this way, the amount of dust generated is continuously measured during converter blowing, and when the amount exceeds an arbitrary set value, suppression measures are taken. There are various suppression measures, but the most sensitive response can be achieved when the following two measures are taken at the same time.

)上吹きランス高さの上昇 通常のランス高さの設定値に対して他の操業要因が大幅
に変わらない程度にランス高さを上昇する。それでもダ
スト発生量が設定値以上となる時には再度ランス高さを
上昇させるとダスト発生量が漸減される。
) Increasing the top blowing lance height The lance height is increased to the extent that other operating factors do not change significantly from the normal lance height setting. If the amount of dust generated still exceeds the set value, the lance height is raised again to gradually reduce the amount of dust generated.

ii)上吹き0!の不活性混合ガス化および混合ガス比
の変更 上吹きガスジェットによる火点を冷却しダストrot制
を図る。設定ダスト債または発生ダスト雇の増加速度に
応じて不活性混合ガス比を変える。ガスの種類によって
は0.と混入ガスの比率を変える。
ii) Top blow 0! Inert mixed gasification and changing of the mixed gas ratio cool the fire point with a top-blown gas jet to achieve dust rot control. Vary the inert gas mixture ratio depending on the set dust bond or rate of increase in generated dust bond. 0 depending on the type of gas. and change the ratio of mixed gas.

不活性混合ガスとして、NZ+ Ar+ cotがあり
、ダスト発生量が低下した後は混合ガスの比率を下げる
か純酸素ガスとしてもよい。
As the inert mixed gas, there is NZ+Ar+cot, and after the amount of dust generation decreases, the ratio of the mixed gas may be lowered or pure oxygen gas may be used.

いずれにしても本発明によるダスト抑制法は冶金特性を
悪化させることなくダスト発生πを連続的に計測し、ダ
スト発生速度が設定上限値以上となった場合に前述のダ
スト抑制のための2つのアクションを同時にとるもので
ある。設定上限値ば吹錬時間を通して一定であっ°ζも
また吹錬時間に応じて変更させてもよい。
In any case, the dust suppression method according to the present invention continuously measures the dust generation π without deteriorating the metallurgical properties, and when the dust generation rate exceeds the set upper limit value, the above-mentioned two dust suppression methods are applied. Actions are taken at the same time. The set upper limit value is constant throughout the blowing time, but °ζ may also be changed depending on the blowing time.

〈実施例〉 以下、本発明の実施例を図面に基づいて説明する。第1
図において、上底吹き転炉1には2BOLの溶鉄2を装
入して、底吹き羽口3からは純0.ガスを溶鉄2中へ吹
込み、また上吹きランス4からは通常は純02ガスを溶
鉄2上へ吹付けて吹錬する。
<Example> Hereinafter, an example of the present invention will be described based on the drawings. 1st
In the figure, 2BOL of molten iron 2 is charged into the top and bottom blowing converter 1, and 0.0BOL of pure molten iron is charged from the bottom blowing tuyere 3. Gas is blown into the molten iron 2, and normally pure 02 gas is blown onto the molten iron 2 from the top blowing lance 4 for blowing.

ランス4に供給される純Otガスはバルブteaによっ
て制御されるがバルブtabを介して不活性ガスを混合
することが可能となっている。
The pure Ot gas supplied to the lance 4 is controlled by a valve tea, but it is possible to mix inert gas through a valve tab.

また、ランス4の高さも変更可能であり、本実施例では
底吹き羽口3から純島ガスを16ONd/蜘、上吹きラ
ンス4から通常純Otガスを550〜750 Nd/幽
吹込んだ、ランス高さはダスト量が設定値以下の場合2
.5mとした。排ガスおよびダストは排ガス煙道5を通
って水冷されたのちそれぞれ分離される。
In addition, the height of the lance 4 can also be changed, and in this example, pure Shima gas was blown in at 16 ONd/gu from the bottom blowing tuyere 3, and normal pure Ot gas was blown in at 550 to 750 Nd/gu from the top blowing lance 4. The lance height is set to 2 when the amount of dust is below the set value.
.. It was set to 5m. The exhaust gas and dust pass through the exhaust gas flue 5, are cooled with water, and then separated.

排ガス流量は煙道5の下流で計測する。すなわち煙道5
の途中で排ガスおよびダストを吸引管6で吸引し、ダス
ト濃度計7に導きダスト発生量を計測する。ダスト濃度
計7は光nk乱方式である。
The exhaust gas flow rate is measured downstream of the flue 5. i.e. flue 5
During the process, exhaust gas and dust are sucked in by a suction pipe 6 and introduced into a dust concentration meter 7 to measure the amount of dust generated. The dust concentration meter 7 is of a light nk scattering type.

ダスト濃度計7で連続的に計測されたダスト濃度と煙道
5の下流に設置された排ガス流量計(図示せず)の値か
らダスト発生速度が連続してダスト発生W検出兼制御゛
計9に表示される。ダスト発生量検出兼制御計9は同時
に制御計の役割を有しており、ダスト発生速度の設定量
または設定パターンに応じてランス高さ変更、上吹きの
混入ガス比変更を指示する。なお8はケーブルを示して
いる。
Based on the dust concentration continuously measured by the dust concentration meter 7 and the value of the exhaust gas flow meter (not shown) installed downstream of the flue 5, the dust generation rate is continuously detected and controlled.Total 9 will be displayed. The dust generation amount detection and control meter 9 also has the role of a control meter, and instructs to change the lance height and the mixed gas ratio for top blowing according to the set amount or set pattern of the dust generation rate. Note that 8 indicates a cable.

上記システムにおいζ得られた本発明例のダスト発生速
度の経時変化を比較例とを併−して第2図に示す、比較
例■では実施例と同様のガス流量でランス高さを2.5
m一定としたところ吹諌開始後徐りにダスト発生量が増
加し、約7分経過から本発明の設定上限値4kg/m/
lを超えた高いレベルでほぼ一定値となり、吹錬後半1
5分頃から低下しはじめる。
Figure 2 shows the change over time in the dust generation rate of the inventive example obtained in the above system along with that of the comparative example.In the comparative example (2), the lance height was set to 2.0 mm at the same gas flow rate as in the example. 5
When m was kept constant, the amount of dust generated gradually increased after the start of blowing, and after about 7 minutes, the upper limit set by the present invention was 4 kg/m/m.
At a high level exceeding l, the value becomes almost constant, and in the second half of blowing 1
It starts to decrease after about 5 minutes.

これに対して実施例ではダスト発生速度4kg/am/
lの設定上限値を超えた時点■で上吹きランス4の純O
tガスにCO!ガスをox/co□=4/1の比率で混
合させると共に溶鉄2の表面からのランス高さは2.5
mから3.0mに上1させ、その状態を■期間継続させ
た。
On the other hand, in the example, the dust generation rate was 4 kg/am/
When the set upper limit of l is exceeded, the pure O of top blowing lance 4 is
CO in t gas! The gases are mixed at a ratio of ox/co□=4/1, and the lance height from the surface of the molten iron 2 is 2.5.
m to 3.0 m, and this state was continued for a period of ■.

これによりダスト発生速度が低下したので引続く■期間
では上吹きランス4のCO□混合を中止すると共にラン
ス4の高さを3.0mから元の2.5mに下降して純島
ガスのみの吹錬を行った。■の期間ではダストの発生速
度が漸増し、再びダスト発生速度が4kg/m/Lに超
えたので上吹きランス4の純0!ガスにArガスをOx
/Ar=3/4の比率で混合すると共にランス4の高さ
を2.5mから2.9mに上昇しその状態でC期間継続
させた。そしてCM間を経過した吹錬末期に通常のラン
ス高さ2.5mに戻したが、吹錬末期であるためダスト
の発生速度は4kg/m/を以下に推移した。
As a result, the dust generation rate decreased, so in the following period ■, CO□ mixing in the top blowing lance 4 was discontinued, and the height of the lance 4 was lowered from 3.0 m to the original 2.5 m, so that only pure island gas could be used. We performed blowing. During the period (2), the dust generation rate gradually increased, and the dust generation rate exceeded 4 kg/m/L again, so the top blowing lance 4 was pure 0! Add Ar gas to the gas
While mixing at a ratio of /Ar=3/4, the height of the lance 4 was raised from 2.5 m to 2.9 m, and period C was continued in this state. Then, at the end of the blowing period after the CM period, the lance height was returned to the normal height of 2.5 m, but since it was the end of the blowing period, the dust generation rate remained below 4 kg/m/.

なお比較例■は実施例と同じ送酸パターンで行い、まず
■の時点でランス高さのみを2.5mから3.0mまで
上げた。しかし、ダスト発生量は設定上限値以下となら
なかった。そこで■の時点でアクシゴンとして上吹き純
島ガスにCO!ガスを3/1の比率で混入させたが、ダ
スト抑制には至らなかった。すなわち、ランス高さ上昇
とH2,Ar。
In Comparative Example (2), the same oxygen supply pattern as in the Example was used, and only the lance height was increased from 2.5 m to 3.0 m at the time of (3). However, the amount of dust generated did not fall below the set upper limit. Therefore, at the time of ■, CO was sent to top-blown Junshima gas as Axigon! Although gas was mixed at a ratio of 3/1, dust was not suppressed. That is, the lance height rise and H2, Ar.

CO2の02への混入を同時に行わなければならないこ
とがわかる。
It can be seen that CO2 must be mixed into 02 at the same time.

以上説明した本発明例と比較例を明確にするために吹I
I!基本条件とその効果を第1表に示す。
In order to clarify the present invention example and comparative example explained above,
I! Table 1 shows the basic conditions and their effects.

第1表から、本発明の方法によれば比較例の方法に比較
して冶金反応に悪影響を与えることなくダストの発生速
度を自在に制御することが可能であり、設定上限値以下
にダスト発生層を抑制できることが分かる。
Table 1 shows that the method of the present invention makes it possible to freely control the dust generation rate without adversely affecting the metallurgical reaction compared to the method of the comparative example, and the dust generation rate can be kept below the set upper limit. It can be seen that the layers can be suppressed.

〈発明の効果〉 以上説明したように本発明の方法によれば、転炉吹錬に
おける排ガス中のダスト発生層が大幅に低減され製鋼歩
留りの向上が図れるき共にダスト処理に費やされる労力
が少なくてすむという効果が得られる。
<Effects of the Invention> As explained above, according to the method of the present invention, the dust generation layer in the exhaust gas during converter blowing can be significantly reduced, the steelmaking yield can be improved, and the labor spent on dust treatment can be reduced. You can get the effect of being able to work.

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

第1図は本発明の実施態様を示す模式図、第2図はダス
ト発生速度の吹錬過程の経時変化を本発明と比較例につ
いて示すグラフである。 5・・・徘ガース煙道、 6・・・tJPガスおよびダスト吸引管、7・・・ダス
ト濃度計、  8・・・ケーブル、9・・・ダスト発生
攪検出兼制fl計、10・・・バルブ。
FIG. 1 is a schematic diagram showing an embodiment of the present invention, and FIG. 2 is a graph showing changes in dust generation rate over time during the blowing process for the present invention and a comparative example. 5... Wandering girth flue, 6... tJP gas and dust suction pipe, 7... Dust concentration meter, 8... Cable, 9... Dust generation agitation detection and control fl meter, 10... ·valve.

Claims (1)

【特許請求の範囲】[Claims]  転炉吹錬において、排ガス中のダスト発生速度を連続
的に計測し、その計測値がダスト発生速度の設定上限値
を超えたときに酸素ガスを上吹きするためのランスの高
さを上昇すると同時に当該ランスから上吹きする酸素ガ
スに不活性ガスを混合させて吹錬することを特徴とする
転炉吹錬における排ガス中のダスト低減方法。
In converter blowing, the dust generation rate in the exhaust gas is continuously measured, and when the measured value exceeds the upper limit set for the dust generation rate, the height of the lance for upward blowing of oxygen gas is raised. A method for reducing dust in exhaust gas in converter blowing, characterized by simultaneously blowing by mixing an inert gas with oxygen gas blown upward from the lance.
JP30992388A 1988-12-09 1988-12-09 Method for reducing dust in exhaust gas in converter blowing Pending JPH02156012A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30992388A JPH02156012A (en) 1988-12-09 1988-12-09 Method for reducing dust in exhaust gas in converter blowing

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30992388A JPH02156012A (en) 1988-12-09 1988-12-09 Method for reducing dust in exhaust gas in converter blowing

Publications (1)

Publication Number Publication Date
JPH02156012A true JPH02156012A (en) 1990-06-15

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP30992388A Pending JPH02156012A (en) 1988-12-09 1988-12-09 Method for reducing dust in exhaust gas in converter blowing

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Country Link
JP (1) JPH02156012A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6017380A (en) * 1995-01-06 2000-01-25 Nippon Steel Corporation Top-blown refining method in converter featuring excellent decarburization and top-blown lance for converter
JP2014040627A (en) * 2012-08-21 2014-03-06 Kobe Steel Ltd Refining method

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6017380A (en) * 1995-01-06 2000-01-25 Nippon Steel Corporation Top-blown refining method in converter featuring excellent decarburization and top-blown lance for converter
JP2014040627A (en) * 2012-08-21 2014-03-06 Kobe Steel Ltd Refining method

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