JPH01222004A - Method for operating blast furnace - Google Patents
Method for operating blast furnaceInfo
- Publication number
- JPH01222004A JPH01222004A JP4788888A JP4788888A JPH01222004A JP H01222004 A JPH01222004 A JP H01222004A JP 4788888 A JP4788888 A JP 4788888A JP 4788888 A JP4788888 A JP 4788888A JP H01222004 A JPH01222004 A JP H01222004A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- blast
- level
- coke
- flux
- 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
Links
- 238000000034 method Methods 0.000 title abstract description 5
- 239000000571 coke Substances 0.000 claims abstract description 15
- 230000004907 flux Effects 0.000 claims abstract description 10
- 239000002893 slag Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 abstract description 6
- 239000002801 charged material Substances 0.000 abstract 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 18
- 229910052742 iron Inorganic materials 0.000 description 9
- 239000002184 metal Substances 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 238000010586 diagram Methods 0.000 description 5
- 230000008018 melting Effects 0.000 description 4
- 238000002844 melting Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000011017 operating method Methods 0.000 description 3
- 229910000805 Pig iron Inorganic materials 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 238000007664 blowing Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
Abstract
Description
この発明は高炉の長時間休風に入る時、減尺操業により
、休風後の立上りを円滑に実施するための操業方法に関
する。The present invention relates to an operating method for smoothly starting up after a blast furnace by reducing the scale when the blast furnace enters a long-term wind shutdown.
従来より、高炉で100時間以上の長時間休風を実施す
る際は、次のような点に留意した操業方法が行゛なわれ
る。
■ 体風入り時の溶銑温度の確保
■ 休風時、炉内残留装入物の溶解防止■ 炉底残銑滓
の凝固防止
■ 立上り時、炉内残留鉄鉱石の急激な溶解防止
上記の点に留意し、従来は炉内の装入物(コークス士鉄
鉱石+7ラツクス)を通常の操業上ストックレベルで止
める方法と、炉内の装入物を、操業中の鉱石/コークス
を低く、つまりコークス11当りの溶銑生成量(コーク
ス比)を低く抑えた状態で止める方法により、長時間休
風時の立上りの円滑化をはかつていた。Conventionally, when a blast furnace is to be closed for a long time of 100 hours or more, an operating method is used that takes into account the following points. ■ Ensuring the hot metal temperature when entering the body air ■ Preventing the melting of the charge remaining in the furnace during wind breaks ■ Preventing solidification of the pig iron slag remaining at the bottom of the furnace ■ Preventing the rapid dissolution of iron ore remaining in the furnace during start-up The above points In consideration of the By stopping the process while keeping the amount of hot metal produced per coke 11 (coke ratio) low, it has been possible to smooth the start-up during long periods of wind downtime.
しかし、上記従来の方法には次に記載する問題点がめっ
た。
■ 休風時、炉内残留鉄分が溶解する。
■ 炉内残留鉄分が溶解すると、炉底部へ温度の低い溶
銑が滴下し、炉底部の溶銑温度を低下せしめる。
■ 休風中の溶解で発生した溶銑が炉内の残留物中を降
下する際、この炉内残留物の影響により途中で凝固し、
立上り時の障害となる付着物あるいは塊状物を形成する
可能性が多分にある。
■ 立上り直後の非常に重要に局面において、炉下部す
なわち羽口部に近い所で炉内の残留鉄分が急速に溶解し
、羽口部を閉鎖するという事態が発生する。
■ 立上り初期に炉内で発生した温度の低い溶銑が未だ
温度の低い炉底部へ流れ込むことにより、ざらに炉底部
温度を低下せしめ、炉内残銑滓の炉外排出が困難となり
、操業の立上り早期復帰が困難となる。
この発明は従来のこのような問題点を解決するためにな
されたものであり、長時間休風後の立上りを円滑にかつ
短時間に行なうことが可能な操業方法を提案せんとする
ものである。However, the above conventional method has encountered the following problems. ■ During the wind break, residual iron in the furnace dissolves. ■ When the residual iron in the furnace melts, low-temperature hot metal drips to the bottom of the furnace, lowering the temperature of the hot metal at the bottom of the furnace. ■ When the hot metal generated during melting during wind rest falls through the residue in the furnace, it solidifies midway due to the influence of the residue in the furnace.
There is a high possibility that deposits or lumps will form which will be an obstacle during start-up. ■ At a very critical stage immediately after start-up, residual iron in the furnace rapidly dissolves in the lower part of the furnace, that is, near the tuyere, causing the tuyere to close. ■ The low-temperature hot metal generated in the furnace at the beginning of startup flows into the bottom of the furnace, where the temperature is still low, which causes the temperature at the bottom of the furnace to drop rapidly, making it difficult to discharge the residual pig iron slag from the furnace, and causing a drop in the temperature at the start-up of the furnace. Early recovery becomes difficult. This invention was made in order to solve these conventional problems, and aims to propose an operating method that can smoothly and quickly start up after a long period of wind cessation. .
この発明の要旨は、高炉の長時間休風に入る前に、予め
炉内の装入物レベルを高炉下部のボッシュレベルまで減
尺し、炉内の残留物をコークスとスラグ成分調整用フラ
ックスのみとして休風に入ることを特徴とするものであ
る。The gist of this invention is to reduce the charge level in the blast furnace to the Bosch level at the bottom of the blast furnace in advance before the blast furnace is put into a long-term air break, and to reduce the remaining amount in the furnace to only coke and flux for adjusting slag components. It is characterized by entering a period of rest.
この発明において、炉内装入物レベルを高炉下部のボッ
シュレベルまで減尺することとしたのは、休風中の炉内
に可及的に溶解物を残存させておかないためである。た
だし、装入物レベルは吹止めの状態とならないよう羽口
の上部になるようにする必要がある。
また、休風前の炉内残留物をコークスとスラグ調整用フ
ラックスのみとしたのは、休風中の溶解により障害とな
る鉄分を皆無とするためである。
以下、この発明を図面に基づいて説明する。
第1図(A>は減尺操業前の炉内装入物とそのレベルを
示し、同図(B)は減尺操業直前の状態を示し、同図(
C)は休風入り時の炉内装入物状況を示す図である。図
中(3)は羽口である。
すなわち、炉内装入物(コークス+鉄鉱石+フラックス
)(1)を通常操業状態(第1図A)より、減尺操業に
移行する際は、炉内に(コークス+フラックス)(2)
を必要量装入し、その後装入を停止し送風量、炉内散水
等により炉内装入物(1)のレベルを低下させていく(
第1図B)。
この減尺操業により装入物(2)のレベルが高炉の下部
すなわちボッシュ部の目標レベル(羽口の上部)まで到
達すると(第1図C)、通常の休風に入るのである。こ
の時、炉内の残留物は(コークス+フラックス)(2)
のみである。
休風入り後は羽口(3)より空気の侵入を防止するため
仝羽口の閉塞を速やかに実施し、そのまま放置する。
休風後の立上りは、羽口閉塞部の順次開孔と装入物レベ
ルの復帰(増尺)を実施する。
(実 施 例]
A高炉(2700m”)の高炉の減尺操業にこの発明方
法を適用した。その際、炉内装入物レベルをボッシュ部
まで低下させ、また炉内残留物をコークスと7ラツクス
のみとして長時間休風に入った場合の減尺操業実績を第
2図に示す。
第2図より、休風時間が105時間50分の長時間であ
ったにもかかわらず、立上り操業は極めて順調で、送風
後22時間35分の短時間で、通常の送風量諸元まで復
帰させることができた。
ちなみに従来法では、休風時間が100時間以上の場合
、立上りに48時間程度の長時間を要する。
[発明の効果]
以上説明したごとく、この発明方法によれば、次に記載
する効果を奏する。
■ 休風中の炉内装入物中溶銑の溶解を減少させられる
結果、立上り操業の障害となる付着物や塊上物の生成が
極めて少なくなり、休風後の立上り操業の円滑化がはか
られ、立上り時間を大幅に短縮できる。
■ 炉内の残留鉄分により羽口が閉塞されるという事態
も起らない。
■ 立上り初期に炉内の溶銑が炉底部へ流れ込んで炉底
部温度を低下させることもほとんどなくなることにより
、炉内残銑滓の炉外排出も容易となり、操業の立上り早
期復帰が可能となる。
■ 稼動高炉での大規模な設備改造や高炉休止による生
産量調整が、大幅な生産量減を伴うことな〈実施可能と
なる。In this invention, the reason why the level of the contents in the furnace is reduced to the Bosch level at the bottom of the blast furnace is to prevent as much melted material from remaining in the furnace during air rest. However, the level of the charge must be at the top of the tuyere to avoid a blockage condition. Furthermore, the reason why the only residues in the furnace before the wind break were coke and slag adjustment flux was to eliminate any iron content that would be a problem due to melting during the wind break. The present invention will be explained below based on the drawings. Figure 1 (A> shows the contents in the furnace and their levels before the scale reduction operation, Figure 1 (B) shows the state immediately before the scale reduction operation, and Figure 1 (
C) is a diagram showing the state of contents in the furnace at the time of wind break. (3) in the figure is the tuyere. In other words, when transitioning from the normal operating state (Fig. 1 A) to reduced-scale operation, the contents in the furnace (coke + iron ore + flux) (1) are changed to (coke + flux) (2).
Charge the required amount of material (1), then stop charging and reduce the level of the material (1) in the furnace by adjusting the air flow rate, watering inside the furnace, etc.
Figure 1 B). When the level of the charge (2) reaches the target level (upper part of the tuyere) in the lower part of the blast furnace, that is, in the bosch section (Fig. 1C) through this scale reduction operation, a normal wind break begins. At this time, the residue in the furnace is (coke + flux) (2)
Only. After the wind breaks, immediately close the tuyere (3) to prevent air from entering, and leave it as it is. When the wind starts to rise after the wind has stopped, the closed tuyeres are sequentially opened and the charge level is restored (increased). (Example) The method of this invention was applied to the downsizing operation of blast furnace A (2700 m"). At that time, the level of the contents in the furnace was lowered to the Bosch area, and the residual material in the furnace was reduced to coke and 7 lac. Figure 2 shows the results of reduced scale operation when there was a long wind break.From Figure 2, even though the wind break was a long time of 105 hours and 50 minutes, the start-up operation was extremely slow. All went smoothly, and we were able to return to the normal air flow specifications in a short time of 22 hours and 35 minutes after blowing air.Incidentally, with the conventional method, if the air rest time was 100 hours or more, it would take about 48 hours to start up. [Effects of the Invention] As explained above, the method of this invention has the following effects: ■ As a result of reducing the melting of hot metal in the charge in the furnace during wind break, startup operation is possible. The generation of deposits and lumps that can be a nuisance to the furnace is extremely reduced, making start-up operations smoother after a wind break, and the start-up time can be significantly shortened. ■ The tuyere is blocked by residual iron in the furnace. ■ Since there is almost no possibility that the hot metal in the furnace flows into the bottom of the furnace and lowers the temperature at the bottom of the furnace in the early stages of start-up, it becomes easy to discharge the remaining iron slag from the furnace, and the operation can be improved. ■ It becomes possible to make large-scale equipment modifications to operating blast furnaces or adjust production volume by shutting down the blast furnace without significantly reducing production volume.
第1図はこの発明の説明図で、図(A)減尺操業に入る
前の通常のストックレベルまで装入物が存在している状
態を示す図、図(B)は減尺操業直前炉内装入物状態を
示す図、図(C)は休風入り時の炉内装入物状況を示す
図、第2図はこの発明の実施例における減尺操業実績デ
ータを示す図・ である。
1・・・炉内装入物(コークス士鉄鉱石+7ラツクス)
2・・・炉内装入物(コークス+フラッグス)3・・・
羽口
出願人 住友金属工業株式会社Figure 1 is an explanatory diagram of this invention. Figure (A) shows the state where the charge is present up to the normal stock level before starting the reduction operation, and Figure (B) shows the furnace immediately before the reduction operation. Figure (C) is a diagram showing the state of the contents inside the furnace, and Figure (C) is a diagram showing the state of the contents inside the furnace at the time of wind break, and Fig. 2 is a diagram showing actual data of the scale reduction operation in an embodiment of the present invention. 1... Furnace contents (coke iron ore + 7 lux) 2... Furnace contents (coke + flags) 3...
Tuyere applicant Sumitomo Metal Industries, Ltd.
Claims (1)
物レベルを高炉ボッシュレベルまで減尺し、炉内残留物
をコークスとスラグ成分調整用フラックスのみとして休
風に入ることを特徴とする高炉操業方法。In the reduced-scale blowdown operation of a blast furnace, the level of the contents in the furnace is reduced to the blast furnace Bosch level before the wind is shut down, and the furnace enters the wind hiatus with only coke and flux for adjusting the slag components remaining in the furnace. How to operate a blast furnace.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4788888A JPH01222004A (en) | 1988-03-01 | 1988-03-01 | Method for operating blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4788888A JPH01222004A (en) | 1988-03-01 | 1988-03-01 | Method for operating blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01222004A true JPH01222004A (en) | 1989-09-05 |
Family
ID=12787939
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4788888A Pending JPH01222004A (en) | 1988-03-01 | 1988-03-01 | Method for operating blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01222004A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013224474A (en) * | 2012-04-23 | 2013-10-31 | Nippon Steel & Sumitomo Metal Corp | Method of blowing-down of blast furnace with lowering stock |
-
1988
- 1988-03-01 JP JP4788888A patent/JPH01222004A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013224474A (en) * | 2012-04-23 | 2013-10-31 | Nippon Steel & Sumitomo Metal Corp | Method of blowing-down of blast furnace with lowering stock |
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