JPH0694377A - Duct collecting method for ladle refining furnace - Google Patents

Duct collecting method for ladle refining furnace

Info

Publication number
JPH0694377A
JPH0694377A JP24659392A JP24659392A JPH0694377A JP H0694377 A JPH0694377 A JP H0694377A JP 24659392 A JP24659392 A JP 24659392A JP 24659392 A JP24659392 A JP 24659392A JP H0694377 A JPH0694377 A JP H0694377A
Authority
JP
Japan
Prior art keywords
converter
furnace
dust collecting
dust
ladle refining
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
JP24659392A
Other languages
Japanese (ja)
Inventor
Masaya Tobiyachi
雅也 飛矢地
Ryuichi Asaho
隆一 朝穂
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 JP24659392A priority Critical patent/JPH0694377A/en
Publication of JPH0694377A publication Critical patent/JPH0694377A/en
Pending legal-status Critical Current

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  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

PURPOSE:To effectively collect dusts of a ladle refining furnace without newly installing a separate dust collecting facility by refining by the furnace directly under a converter, and effectively utilizing a dust collecting facility attached to the converter to collect powder dusts of the furnace upon refining and to also serve it as a dust collector. CONSTITUTION:A ladle refining furnace 1 contains molten steel and slag 10 therein, and is placed on a conveying truck 12 to be conveyed. On the other hand, a waste gas recovery hood 3, a dust collecting duct 4, an operating deck 5, etc., are attached to a converter 2. In this case, the furnace 1 is refined directly under the converter 2. Powder dusts of the furnace 1 generated upon refining are collected by utilizing the hood 3 and the duct 4 attached to the converter 2. Thus, a period in which a load to be applied to a dust collecting facility of the converter 2 is small and a slag modifying process by the furnace 1 are lapped at timing to be operated, thereby eliminating installation of a new large- sized dust collecting facility.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、取鍋精錬炉の集塵方法
に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust collecting method for a ladle refining furnace.

【0002】[0002]

【従来の技術】近年、鉄鋼材料の介在物に起因する表面
欠陥に対する要求は益々厳格化し、このような要求に対
応すべく種々の清浄化技術が開発されている。この種の
技術の1つとして特公平2−19168号公報、特開平
2−30711号公報に開示されているスラグ改質法に
よる技術がある。すなわち、取鍋精錬炉に受鋼後、スラ
グ改質処理をおこない、ついで真空処理等にかけて溶鋼
の清浄化を図る技術である。この方法では、取鍋精錬炉
に受鋼時にスラグの一部も混入させ、スラグを改質処理
する操作が必要となる。
2. Description of the Related Art In recent years, demands for surface defects caused by inclusions of steel materials have become increasingly severe, and various cleaning techniques have been developed to meet such demands. As one of the techniques of this type, there is a technique based on the slag reforming method disclosed in Japanese Patent Publication No. 2-19168 and Japanese Patent Laid-Open No. 30711/1990. That is, this is a technique for purifying molten steel by subjecting a ladle refining furnace to steel, performing slag reforming treatment, and then performing vacuum treatment or the like. According to this method, it is necessary to mix a part of the slag into the ladle refining furnace at the time of steel reception to modify the slag.

【0003】しかし、スラグ改質処理はフラックス等の
添加、攪拌を伴うため、著しい発煙を伴うことは避けら
れない。但し、スラグ改質処理の実際の所要時間は、例
えば特開平2−30711号公報に開示されているよう
に、5分前後である。つまり、短時間に大量の粉塵を発
生することが、取鍋精錬炉によるスラグ改質処理の特徴
である。したがってその集塵には、従来の集塵設備では
対処できず、新たに大型の集塵設備の設置を必要とす
る。
However, since the slag reforming treatment involves the addition of flux and the like and stirring, it is unavoidable that significant smoke is generated. However, the actual time required for the slag reforming treatment is around 5 minutes as disclosed in, for example, Japanese Patent Laid-Open No. 2-30711. That is, generation of a large amount of dust in a short time is a characteristic of the slag reforming process by the ladle refining furnace. Therefore, the dust collection cannot be dealt with by the conventional dust collection equipment, and it is necessary to newly install a large dust collection equipment.

【0004】他方、転炉の排ガス回収設備および/また
は集塵設備(以下転炉の集塵設備と略す。)の稼働状況
を調査すると、出鋼後は排滓、炉体ライニングの整備、
原料装入等の作業があり、また、吹酸を開始してもその
初期、すなわち、脱炭速度が時間とともに上昇する時期
は、溶鋼温度も低く排ガス量は比較的少ない。すなわ
ち、取鍋精錬炉に出鋼後の5〜10分前後は転炉の集塵
設備にかかる負荷が比較的に少ない時期である。
On the other hand, when the operating conditions of the exhaust gas recovery equipment and / or dust collecting equipment of the converter (hereinafter abbreviated as the dust collecting equipment of the converter) are investigated, after the tapping, the slag and the furnace body lining are
There are operations such as charging of raw materials, and even after the start of blowing acid, the molten steel temperature is low and the amount of exhaust gas is relatively small at the initial stage, that is, at the time when the decarburization rate rises with time. That is, about 5 to 10 minutes after tapping in the ladle refining furnace, the load on the dust collecting equipment of the converter is relatively small.

【0005】また、転炉の集塵設備としては通常、1
0,000〜20,000m3 /min程度の排ガス処
理能力を有する設備が設置されている。(鉄鋼便覧2
(第3版)p.463、日本鉄鋼協会編)
In addition, the dust collecting equipment of the converter is usually 1
Equipment having an exhaust gas treatment capacity of about 20,000 to 20,000 m 3 / min is installed. (Steel Manual 2
(3rd edition) p. 463, edited by Japan Iron and Steel Institute)

【0006】[0006]

【発明が解決しようとする課題】本発明は、以上のよう
な技術の現状にかんがみてなされたものであって、転炉
の集塵設備を有効に利用することによって、新たに大型
の集塵設備を設置することなく、充分な集塵をおこなう
ことのできる取鍋精錬炉の集塵方法を提供することを目
的としてなされたものである。
SUMMARY OF THE INVENTION The present invention has been made in view of the current state of the art as described above, and by effectively utilizing the dust collecting equipment of a converter, a new large dust collecting apparatus can be obtained. The object of the present invention is to provide a method for collecting dust in a ladle refining furnace that can perform sufficient dust collection without installing equipment.

【0007】[0007]

【課題を解決するための手段】本発明は、取鍋精錬炉に
よる精錬を転炉直下で行い、該転炉の集塵設備を用いて
集塵することを特徴とする取鍋精錬炉の集塵方法であ
る。
DISCLOSURE OF THE INVENTION According to the present invention, a ladle refining furnace is characterized in that refining by a ladle refining furnace is performed directly under a converter and dust is collected by using a dust collecting facility of the converter. It is a dust method.

【0008】[0008]

【作用】本発明では、転炉の集塵設備にかかる負荷が少
ない時期と、取鍋精錬炉によるスラグ改質処理とを、時
間的にラップさせて操業するようにし、さらにその操業
場所を転炉の集塵設備が作用する転炉直下としたので、
新たに大型の集塵設備を設置することは不要となる。
In the present invention, the time when the load on the dust collecting equipment of the converter is low and the slag reforming treatment by the ladle refining furnace are time-lapped and the operation place is changed. Since it was directly under the converter where the dust collection equipment of the furnace works,
It is not necessary to install new large-scale dust collection equipment.

【0009】なお、ここで転炉直下とは、必ずしも転炉
の直下のみならず、転炉の集塵設備の集塵作用が作用す
る範囲の場所のことを意味する。
The term "directly below the converter" as used herein means not only immediately below the converter but also within a range where the dust collecting action of the dust collecting equipment of the converter operates.

【0010】[0010]

【実施例】図1は実施例1のArバブリングによるスラ
グ改質処理時の集塵状態をしめす縦断面図、図2は比較
例1のArバブリングによるスラグ改質処理時の集塵状
態をしめす縦断面図、図3は実施例および比較例の転炉
と取鍋精錬炉の配置、および環境粉塵濃度の各測定点
、、、、およびの位置をしめす平面図、図
4は実施例1および比較例1、3の各測定点における環
境粉塵濃度の測定値をしめすグラフである。
EXAMPLE FIG. 1 is a vertical cross-sectional view showing a dust collection state during slag reforming treatment by Ar bubbling in Example 1, and FIG. 2 shows a dust collection state during slag reforming treatment by Ar bubbling in Comparative Example 1. FIG. 3 is a vertical sectional view, FIG. 3 is a plan view showing the arrangement of converters and ladle refining furnaces of Examples and Comparative Examples, and the measurement points of environmental dust concentration ,,, and FIG. It is a graph which shows the measured value of the environmental dust density in each measurement point of Comparative Examples 1 and 3.

【0011】図1〜3で、1は取鍋精錬炉、2は転炉、
3は転炉に付属する排ガス回収フード、4は集塵機につ
らなる転炉の集塵ダクト、5は転炉の作業デッキ、6は
転炉のトラニオン軸、7は転炉操作室、8は実施例の取
鍋精錬炉の位置(転炉直下)を点線でしめし、9は比較
例の取鍋精錬炉の位置(Arバブリング場)を点線でし
めしたものである。また、10は取鍋精錬炉内の溶鋼、
溶滓、11は発生する取鍋精錬炉の粉塵を、12は取鍋
搬送台車をしめしたものである。なお、Arバブリング
設備は図示を省略した。
1 to 3, 1 is a ladle refining furnace, 2 is a converter,
3 is an exhaust gas recovery hood attached to the converter, 4 is a dust collecting duct of the converter connected to a dust collector, 5 is a working deck of the converter, 6 is a trunnion shaft of the converter, 7 is a converter operating room, and 8 is an embodiment. The dotted line indicates the position of the ladle refining furnace (immediately below the converter), and 9 indicates the position of the ladle refining furnace of the comparative example (Ar bubbling field) by the dotted line. Also, 10 is molten steel in the ladle refining furnace,
The slag, 11 is dust generated in the ladle refining furnace, and 12 is a ladle carrier truck. The Ar bubbling equipment is not shown.

【0012】転炉から取鍋精錬炉内に出鋼後、スラグ改
質処理を実施した。スラグ改質処理剤は、いずれもアル
ミ灰を使用し、溶滓5kgについて1kg添加した。な
お、実施例1、2はいずれも転炉の集塵設備を稼働しな
がら処理した。このときのスラグ改質処理の有無、スラ
グ改質処理の場所およびArバブリングの有無を、実施
例1、2、および比較例1、2として表1にまとめてし
めした。なお、Arバブリング場は転炉直下から約17m
離れた位置にある。
After tapping the steel from the converter into the ladle refining furnace, slag reforming treatment was carried out. Aluminum ash was used as the slag modifier, and 1 kg was added per 5 kg of slag. In each of Examples 1 and 2, the treatment was performed while operating the dust collecting equipment of the converter. The presence / absence of the slag reforming treatment, the location of the slag reforming treatment and the presence / absence of Ar bubbling at this time are summarized in Table 1 as Examples 1 and 2 and Comparative Examples 1 and 2. The Ar bubbling alley is about 17m from directly under the converter.
Located in a remote location.

【0013】このときの転炉付近の各測定点の環境粉塵
濃度の測定結果も表1にしめした。
Table 1 also shows the measurement results of the environmental dust concentration at each measuring point near the converter at this time.

【0014】[0014]

【表1】 [Table 1]

【0015】測定点は図3にしめすように、最も転炉か
ら離れた測定点、で転炉直下から約9mの位置であ
る。図4から、Arバブリング場でArバブリングしな
がらスラグ改質処理を実施した比較例1の場合、環境粉
塵濃度の最大値が測定点で22.25mg/m3に達
するのに対して、転炉直下でArバブリングし、かつ、
転炉の集塵設備を稼働しながらスラグ改質処理を実施し
た実施例1では、環境粉塵濃度の最大値が測定点で
0.82mg/m3 に低下しており、スラグ改質処理お
よびArバブリング処理を実施しない比較例3とほぼ同
程度の環境粉塵濃度をしめすことがわかる。
As shown in FIG. 3, the measurement point is the farthest measurement point from the converter, and is a position approximately 9 m from directly below the converter. From FIG. 4, in the case of Comparative Example 1 in which the slag reforming treatment was performed while Ar bubbling in the Ar bubbling field, the maximum value of the environmental dust concentration reached 22.25 mg / m 3 at the measurement point, while the converter Ar bubbling directly below, and
In Example 1 in which the slag reforming treatment was carried out while operating the dust collecting equipment of the converter, the maximum value of the environmental dust concentration decreased to 0.82 mg / m 3 at the measurement point. It can be seen that the environmental dust concentration is almost the same as that of Comparative Example 3 in which the bubbling treatment is not performed.

【0016】なお、比較例3は、スラグ改質処理もAr
バブリング処理も伴わない、通常の取鍋溶鋼処理をAr
バブリング場で実施したときの測定結果で、本発明の効
果を明瞭ならしめるために併記した。また、実施例1で
は、実公昭58−2528号公報に開示されたAr供給
ホースおよび取鍋底吹きバブリング装置を搭載した受鋼
台車上でスラグ改質処理を実施する方法を採用して処理
サイクルの短縮につとめた。
In Comparative Example 3, the slag reforming treatment was performed using Ar.
Normal ladle molten steel treatment without bubbling treatment Ar
The results of the measurement performed at the bubbling alley are also shown in order to clarify the effect of the present invention. In addition, in Example 1, the method of performing the slag reforming treatment on the steel receiving trolley equipped with the Ar supply hose and the ladle bottom blowing bubbling device disclosed in Japanese Utility Model Publication No. 58-2528 was adopted and the treatment cycle was changed. I tried to shorten it.

【0017】また、実施例2は、転炉直下で、転炉の集
塵設備を稼働しながら、Arバブリングなしで、機械攪
拌によるスラグ改質処理を実施した例であり、比較例2
のArバブリング場で、Arバブリングなしで、機械攪
拌によるスラグ改質処理を実施した場合の環境粉塵濃度
と比較して大幅に低下している。すなわち、比較例2の
環境粉塵濃度の最大値が測定点で21.75mg/m
3 に達するのに対して、実施例2では、環境粉塵濃度の
最大値が測定点で0.80mg/m3 に達しているに
過ぎない。
Further, Example 2 is an example in which the slag reforming treatment by mechanical stirring was carried out directly under the converter while operating the dust collecting equipment of the converter without Ar bubbling, and Comparative Example 2
In the Ar bubbling field, the environmental dust concentration is significantly lower than the environmental dust concentration when the slag reforming treatment is performed by mechanical stirring without Ar bubbling. That is, the maximum environmental dust concentration of Comparative Example 2 was 21.75 mg / m 2 at the measurement point.
On the other hand, in Example 2, the maximum value of the environmental dust concentration reaches 0.80 mg / m 3 at the measurement point.

【0018】以上の結果から明らかなように、本発明の
効果は、攪拌装置の如何にかかわらず発揮することが分
かる。なお、エアカーテン等の公知のシール設備、ある
いは従来の既設の小型の集塵設備を併用すれば、本発明
の効果を一層向上することができる。また、本発明の集
塵方法は、スラグ改質処理にかぎらず、短時間に大量の
粉塵を発生する取鍋精錬炉による処理には全て適用する
ことができる。
As is clear from the above results, the effects of the present invention are exhibited regardless of the stirring device. The effect of the present invention can be further improved by using a known sealing facility such as an air curtain or a conventional existing small dust collecting facility. Further, the dust collecting method of the present invention can be applied not only to the slag reforming treatment but also to the treatment by the ladle refining furnace that generates a large amount of dust in a short time.

【0019】[0019]

【発明の効果】本発明の取鍋精錬炉の集塵方法による
と、転炉の集塵設備を有効に利用できるように構成した
ので、新たに集塵設備を設置することなく、充分な集塵
効果を得ることができる。
According to the dust collecting method of the ladle refining furnace of the present invention, since the dust collecting equipment of the converter can be effectively used, it is possible to sufficiently collect dust without installing new dust collecting equipment. The dust effect can be obtained.

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

【図1】実施例1のArバブリングによるスラグ改質処
理時の集塵状態をしめす縦断面図である。
FIG. 1 is a vertical cross-sectional view showing a dust collecting state during a slag reforming process by Ar bubbling in Example 1.

【図2】比較例1のArバブリングによるスラグ改質処
理時の集塵状態をしめす縦断面図である。
FIG. 2 is a vertical cross-sectional view showing a dust collecting state during a slag reforming treatment by Ar bubbling in Comparative Example 1.

【図3】実施例および比較例の転炉と取鍋精錬炉の配
置、および環境粉塵濃度の測定点の位置をしめす平面図
である。
FIG. 3 is a plan view showing the arrangement of converters and ladle refining furnaces of Examples and Comparative Examples, and the positions of measurement points for environmental dust concentration.

【図4】実施例1および比較例1、3の各測定点におけ
る環境粉塵濃度の測定値をしめすグラフである。
FIG. 4 is a graph showing measured values of environmental dust concentration at each measurement point in Example 1 and Comparative Examples 1 and 3.

【符号の説明】[Explanation of symbols]

1 取鍋精錬炉 2 転炉 3 転炉の排ガス回収フード 4 転炉の集塵ダクト 5 転炉の作業デッキ 6 転炉のトラニオン軸 7 転炉操作室 8 実施例の取鍋精錬炉の位置(転炉直下) 9 比較例の取鍋精錬炉の位置(Arバブリング場) 10 溶鋼、溶滓 11 取鍋精錬炉の粉塵 12 取鍋搬送台車 1 ladle refining furnace 2 converter 3 exhaust gas recovery hood of converter 4 converter dust collection duct 5 converter working deck 6 converter trunnion shaft 7 converter operating room 8 position of ladle refining furnace of example ( Directly below the converter) 9 Position of ladle refining furnace of comparative example (Ar bubbling field) 10 Molten steel, slag 11 Dust of ladle refining furnace 12 Ladle carrier

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】取鍋精錬炉による精錬を転炉直下で行い、
該転炉に付属する排ガス回収設備および/または集塵設
備を用いて集塵することを特徴とする取鍋精錬炉の集塵
方法。
[Claim 1] The refining by a ladle refining furnace is performed directly under the converter,
A method for collecting dust in a ladle refining furnace, comprising collecting dust using an exhaust gas recovery facility and / or a dust collecting facility attached to the converter.
JP24659392A 1992-09-16 1992-09-16 Duct collecting method for ladle refining furnace Pending JPH0694377A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24659392A JPH0694377A (en) 1992-09-16 1992-09-16 Duct collecting method for ladle refining furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24659392A JPH0694377A (en) 1992-09-16 1992-09-16 Duct collecting method for ladle refining furnace

Publications (1)

Publication Number Publication Date
JPH0694377A true JPH0694377A (en) 1994-04-05

Family

ID=17150729

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24659392A Pending JPH0694377A (en) 1992-09-16 1992-09-16 Duct collecting method for ladle refining furnace

Country Status (1)

Country Link
JP (1) JPH0694377A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6790494B2 (en) 2001-05-15 2004-09-14 Nippon Sheet Glass Co., Ltd. Heat insulating and shielding glass panel
KR101149168B1 (en) * 2009-06-26 2012-05-25 현대제철 주식회사 Apparatus and method for controlling a damper of duct in ladle furnace
CN105135899A (en) * 2015-09-28 2015-12-09 云南云铝涌鑫铝业有限公司 Intermediate frequency furnace

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6790494B2 (en) 2001-05-15 2004-09-14 Nippon Sheet Glass Co., Ltd. Heat insulating and shielding glass panel
KR101149168B1 (en) * 2009-06-26 2012-05-25 현대제철 주식회사 Apparatus and method for controlling a damper of duct in ladle furnace
CN105135899A (en) * 2015-09-28 2015-12-09 云南云铝涌鑫铝业有限公司 Intermediate frequency furnace
CN105135899B (en) * 2015-09-28 2017-09-29 云南云铝涌鑫铝业有限公司 Intermediate frequency furnace

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